CHAPTER Env-Wq 700
STANDARDS OF DESIGN AND CONSTRUCTION FOR
SEWERAGE AND WASTEWATER TREATMENT FACILITIES
Statutory
Authority: RSA 485-A:6, III
Revision Note:
Document #8590, effective 3-25-06, readopted with
amendments and redesignated former Chapter Env-Ws 700 titled Standards of
Design and Construction for Sewerage and Wastewater Treatment Facilities as
Env-Wq 700 pursuant to a rules reorganization plan for Department rules
approved by the Director of the Office of Legislative Services on 9-7-05.
The prior filings for former Env-Ws 700 include the
following documents:
#757, eff 2-18-76
#2245, eff 12-31-82
#2670, eff 4-12-84
#4860, eff 7-5-90; EXPIRED 7-5-96
#6350, INTERIM, eff 10-5-96, EXPIRED
2-2-97
#6590, eff 9-26-97
#8434, INTERIM, eff 9-26-05, EXPIRES: 3-25-06
PART Env-Wq 701
PURPOSE AND APPLICABILITY
Env-Wq
701.01 Purpose. The purpose of this chapter is to protect
public health and the environment by establishing minimum technical standards
and requirements for the planning, design, and construction of sewerage and wastewater treatment facilities, including
solids handling and disposal facilities.
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Env-Wq
701.02 Applicability.
(a) Env-Wq 700 shall apply to any person that
designs or constructs new sewerage, wastewater treatment, or solids handling
and disposal facilities or any appurtenances related thereto.
(b) For purposes of proposed upgrades or other
modifications to existing sewerage, wastewater treatment, or solids handling
and disposal facilities or any appurtenances related thereto, the following
provisions shall apply:
(1) Env-Wq 702
relative to definitions;
(2) Env-Wq 703
relative to engineering design documents; and
(3) All
provisions of Env-Wq 704 through Env-Wq 719 that directly apply to the
system(s) proposed to be upgraded or modified.
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PART Env-Wq 702 DEFINITIONS
Env-Wq 702.01 “Annual average design flow” means the entire volume of
flow, including all infiltration and inflow (I/I), discharged in one year,
expressed as a daily rate.
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Env-Wq 702.02 “Beneficial use” means “beneficial use” as
defined in Env-Wq 802.
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Env-Wq 702.03 “Biochemical oxygen demand (BOD5)”
means the amount of oxygen used by microorganisms in the biochemical oxidation
of decomposable organic matter under aerobic conditions over a 5-day period, as
expressed in milligrams per liter (mg/L).
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Env-Wq 702.04 “Clean Water Act (CWA)” means the Federal
Clean Water Act, Pub. L. 92-500 as amended by Pub. L. 95-217, Pub. L. 95-576,
Pub. L. 96-483, Pub. L. 97-117, Pub. L. 100-4, and 33 U.S.C. 1251 et seq.
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Env-Wq 702.05 “Collector sewer” means a lateral sewer
installed primarily to collect wastewater directly from individual building
sewers or private property.
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Env-Wq 702.06 “Cross-country locations” means locations not
otherwise defined as roadway locations.
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Env-Wq 702.07 “Department” means the New Hampshire
department of environmental services.
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Env-Wq 702.08 “Discharge permit” means a national pollutant
discharge elimination system (NPDES) permit or a New Hampshire groundwater
discharge permit.
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Env-Wq 702.09 “Engineer” means the engineer of the owner,
acting individually or through duly-authorized representatives.
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Env-Wq 702.10 “HS-20 loading” means the force imposed by a
pair of 16,000 pound concentrated loads, one located over the point in question
and the other located 72 inches distant, so as to simulate the tire loads of a
truck.
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Env-Wq 702.11 “Industrial waste” means “industrial waste”
as defined by RSA 485-A:2, VI, as reprinted in Appendix C.
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Env-Wq 702.12 “Interceptor sewer” means a sewer designed to
collect wastewater from collector sewers and transport it to a wastewater
treatment plant.
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Env-Wq 702.13 “Local
legislative body” means “legislative body” as defined by RSA 21:47, as
reprinted in Appendix C.
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Env-Wq 702.14
“Maximum daily flow” means the largest volume of flow anticipated to
occur during a 24-hour period.
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Env-Wq 702.15 “Maximum monthly flow” means the largest
volume of flow anticipated to occur during a continuous 30-day period,
expressed as a daily rate.
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Env-Wq 702.16 “Minimum daily flow” means the smallest
volume of flow anticipated to occur during a 24-hour period.
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Env-Wq 702.17 “Minimum monthly flow” means the smallest
volume of flow anticipated to occur during a continuous 30-day period,
expressed as a daily rate.
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Env-Wq 702.18 “Municipality” means a city, town, district,
county, or other public body created under state law and having jurisdiction
over treatment and disposal of wastewater.
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Env-Wq 702.19 “National Electric Code (NEC)” means the
National Electric Code as adopted under RSA 155-A:1, IV and RSA 155-A:2, I.
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Env-Wq 702.20 “Owner” means the municipality or private
owner for which sewerage or wastewater treatment facilities are designed or
constructed.
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Env-Wq 702.21 “Peak instantaneous flow” means the maximum
anticipated instantaneous flow expressed in gallons per minute (gpm).
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Env-Wq 702.22 “Peak hourly flow” means the largest volume of
flow anticipated to occur during a one-hour period, expressed in gpm.
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Env-Wq 702.23 “Person” means “person” as defined in RSA
485-A:2, IX, as reprinted in Appendix C.
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Env-Wq 702.24 “Pressure
sewer” means a system of individual grinder pumps connected using small
diameter collector sewers to grind, collect, and convey sewage to an interceptor
sewer or a wastewater treatment plant.
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Env-Wq 702.25 “Privately owned” means ownership by a person
other than a municipality.
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Env-Wq
702.26 “Roadway locations” means all
parking lots, traveled ways, and roadway shoulders.
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Env-Wq 702.27 “Sewage” means “sewage” as defined in RSA
485-A:2, X, as reprinted in Appendix C.
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Env-Wq 702.28 “Sewer” means a pipe or conduit used to
convey sewage.
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Env-Wq 702.29 “Sewer appurtenances” means components of a
sewer other than pipe, such as manholes, tees, wyes, chimneys, cleanouts, and
siphons.
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Env-Wq 702.30 “Sewerage” means a system of pipes, pumping
facilities, and appurtenances for the collection and conveyance of sewage and
liquid wastes.
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Env-Wq 702.31 “Standard scale” means the commonly used
drafting scales of engineers and architects including, but not limited to,
1:10, 1:20, 1:40, 1:50, 1:100, and 1/8 inch, 1/4 inch, 3/8 inch, 1/2 inch, 3/4
inch,
and 1 inch to the foot.
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Env-Wq 702.32 “Standard dimension ratio (SDR)” means the
ratio of outside pipe diameter to pipe wall thickness, as used in the pipe
manufacturing industry.
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Env-Wq 702.33 “Total suspended solids (TSS)” means solids
that either float on the surface of, or are in suspension in, water, sewage, or
other liquids, and which are removable by a 0.45 micron filter.
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Env-Wq 702.34 “Wastewater treatment plant (WWTP)” means
“wastewater treatment plant” as defined by RSA 485-A:2, XVI-a, as reprinted in
Appendix C. The term does not include
conventional septic tank and leach field systems as regulated under RSA
485-A:29.
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PART Env-Wq 703
ENGINEERING DESIGN DOCUMENTS
Env-Wq 703.01
Submittal of Design Drawings, Technical Specifications, and
Supporting Documentation.
(a) The owner shall submit design drawings,
technical specifications, and supporting documentation for proposed new or
modified publicly or privately owned sewerage and
WWTPs to the department for approval in accordance with this part.
(b) In addition to (a) above, the owner shall
submit an application for a sewer connection permit to the department for any
proposed sewer,
pursuant to
the requirements of Env-Wq 703.07(a).
(c) All design drawings, technical
specifications, and supporting documentation submitted to the department for
review and approval shall be:
(1) Prepared or
reviewed by an engineer licensed in the state of New
Hampshire pursuant to RSA 310-A:2 through RSA 310-A:27;
(2) Stamped and
signed by the engineer who prepared or reviewed them; and
(3) Accompanied
by a summary transmittal letter that includes:
a. The name and
address of the engineering firm and engineer responsible for design;
b. A brief
description of the project scope;
c. A statement
by the engineer that the plans and specifications are in substantial compliance
with the Env-Wq 700 requirements, with the exception of any waiver requests,
which shall be identified and listed in this letter; and
d. The
signature and seal of the engineer responsible for design.
(d) The owner shall submit the following number
of sets of plans, design drawings, technical specifications, and supporting
documentation:
(1) For state-
or federally-funded projects:
a. For initial
review, 2 printed sets; and
b. For final
review and approval, one complete printed set, 2 additional printed copies of
the cover sheet, and 2 electronic sets submitted on 2 separate compact disks or
DVDs; and
(2) For other
projects:
a. For initial
review, one printed set; and
b. For final
review, one complete printed set, 2 additional printed copies of the cover
sheet, and 2 electronic sets submitted on 2 separate compact disks or DVDs.
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Env-Wq
703.02 Technical Specifications and
Supporting Documentation.
(a) Complete technical specifications and
supporting documentation for the construction of sewerage
and WWTPs shall accompany the design drawings submitted pursuant to Env-Wq
703.01.
(b) The technical specifications shall describe
the following information as applicable to the proposed project:
(1) All
construction information not shown on the drawings that is necessary to inform
the contractor of the design requirements and the quality of materials,
workmanship, and fabrication of the project;
(2) The type,
size, operating characteristics, and rating requirements of all mechanical and
electrical equipment;
(3) Laboratory
fixtures and equipment;
(4) Operating
tools;
(5) Pipe and
other construction materials;
(6) Special
filter materials;
(7) Sewer
appurtenances;
(8) Chemicals
that will be used as part of the wastewater treatment process;
(9)
Instructions for testing materials and equipment as necessary to meet
design standards; and
(10)
Performance tests for the completed works and component units.
(c) The supporting documentation shall include:
(1) For all
projects:
a. Soil
investigations, borings, and geotechnical reports;
b. Flotation
calculations for buried structures; and
c. Design flood
elevations determined in accordance with Env-Wq 706.03; and
(2) For
sewerage and sewage pump station projects, design calculations for:
a. Determination
of the average daily flow, peak hourly flow, and infiltration allowance;
b. Flow velocities
and depths within gravity sewers and channels;
c. System head curves
for force mains and pump capacity curves for all anticipated pump station
operating conditions; and
d. Pump cycle
times, wet well volume requirements, and sewage retention times of wet wells
and force mains.
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Env-Wq 703.03 Design Drawings.
(a) All design drawings shall
include the following information:
(1) A title
citing the project name, location, and owner;
(2) The scale;
(3) The north
arrow;
(4) The name
and signature of the engineer, and the imprint or stamp of their New
Hampshire professional
engineering
license seal;
(5) The date of
the original issue and all revisions;
(6) The
initials of the designer, draftsperson, checker, and responsible engineer;
(7) The
dimensions and relative elevations of all structures;
(8) The
locations and outlines of all mechanical equipment;
(9) The
locations and sizes of all piping;
(10) Water
levels;
(11) Existing
and proposed ground elevations;
(12) A
topographic map of the proposed project site;
(13) The date
and source of survey data; and
(14) Plan sheet
match lines for plan and profile views when more than
one sheet is required for the design drawings.
(b) The design drawings shall be clear, legible,
and drawn to a standard scale which permits all necessary information to be
plainly shown.
(c) The design drawings shall not be larger than
24 inches by 36 inches in dimension.
(d) A vertical datum shall be indicated and, if
different from the national geodetic vertical datum of the United States
Geological Survey (USGS), its relationship thereto shall be noted.
(e) For any test borings:
(1) The
locations of the test borings shall be shown on the plans; and
(2) Boring logs
and soils sampling protocol shall be included in the specifications.
(f) The design drawings shall include plan views,
elevations, sections, and supplementary views which, together with the
specifications and general layouts, provide the working information for the
contract and construction of the works.
(g) The following information shall be submitted
by the engineer:
(1) A location
plan showing the location of all parts of the project with respect to municipal
boundaries and the location and extent of the tributary area within the project
area;
(2) Detail plan
and profile sheets of all proposed sewerage;
(3) Details of
construction of manholes, siphons, and other sewer appurtenances;
(4) General and
detail plans for WWTPs and sewage pumping stations; and
(5) Technical
specifications for all proposed construction.
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Env-Wq 703.04 Design Drawings for Sewerage. Design drawings for proposed sewerage shall,
in addition to meeting the applicable requirements of Env-Wq 703.01 through
Env-Wq 703.03, include the following:
(a) Contour lines at 2-foot intervals and
elevation of existing and proposed project area;
(b) The locations of all streams and other
surface waters within the proposed project area, including their direction of
flow and water surface elevations at the time of survey;
(c) 100-year flood elevations, if available;
(d) The boundary lines of the municipality, sewer
district, or other area to be sewered;
(e) The location, size, and direction of flow of
all existing and proposed sewers;
(f) Insets and detail sections with the scale
shown directly beneath their subtitles;
(g) Plan and profile views in which the plan view
is placed at the top;
(h) Plans clearly showing the location of:
(1) All
existing structures affecting the project;
(2) Existing
and proposed sewer outlets or overflows; and
(3) All other
utilities in the vicinity of the proposed sewerage;
(i) The locations of
existing, proposed, and future sewerage as differentiated by appropriate
symbols or designations;
(j) All topographical symbols and conventions as
employed by the USGS;
(k) The horizontal distance or stationing between
manholes, grades in feet per foot, and sewer sizes, types, and class;
(l) All sewer appurtenances depicted by symbols
and referenced by a legend, with detail drawings of all sewer appurtenances
accompanying the detail sewerage plans;
(m) Profiles indicating:
(1) All
manholes with manhole identification numbers;
(2) Existing
and proposed water main crossings with elevations;
(3) Siphons;
(4) Sewage
pumping stations; and
(5) In the case
of stream crossings, the elevations of stream beds, flow lines, and the type of
pipe;
(n) The sizes and gradients of sewers, surface
elevations, first floor house elevations, and sewer inverts shown at or between
each manhole;
(o) Finish grade elevations;
(p) Elevations of manhole inverts shown to the
nearest 0.01 foot;
(q) All elevations referenced
to a standard datum that is indicated on the plans; and
(r) As specified by the engineer, any special
precautions or methods of construction necessary to prevent surface water
pollution.
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Env-Wq 703.05 Design Drawings for Sewage Pumping
Stations. Design drawings for
proposed sewage pumping stations shall, in addition to meeting the applicable
requirements of Env-Wq 703.01 through Env-Wq 703.04, include the following:
(a) Existing sewage pumping
station locations and elevations;
(b) The location(s) and elevation(s) of all
proposed sewage pumping station(s), including provisions for installation of
future pump(s) if required to meet full build-out of the service area; and
(c) If applicable, 100-year and 500-year flood
elevations.
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Env-Wq
703.06 WWTP Plans. Design drawings for proposed WWTPs or
modifications to existing WWTPs shall, in addition to meeting the applicable
requirements of Env-Wq 703.01 through Env-Wq 703.05, include the following:
(a) A location plan that shows the WWTP in
relation to the sewerage, including topographic
features to indicate its location in relation to streams and the point of
effluent discharge; and
(b) Layouts of the proposed WWTP or proposed
modifications to an existing WWTP that include the following:
(1) Topography
of the site using 2-foot contours;
(2) Dimensions,
elevations, and location of all existing and proposed WWTP structures;
(3) Site
boundaries including areas reserved for future expansion and all buildings or building lots within 600 feet of WWTP property;
(4) A process
and instrumentation diagram showing the flow of sewage, sidestream
flows, and sludge through the WWTP units;
(5) Piping,
including any arrangements for bypassing individual units and the materials
handled and direction of flow through pipes;
(6) Hydraulic
profiles showing the annual average, maximum day, and peak instantaneous flow
elevations;
(7) The high
and low water level elevations of the water body to which the WWTP effluent
discharges or is proposed to discharge;
(8) A summary
of WWTP and unit process design criteria, capacity, and sizing; and
(9) A
description of any features not otherwise covered by the technical
specifications or reports.
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Env-Wq
703.07 Sewer Connection Permit.
(a) In addition to any other local or state
requirements, any person proposing to construct or modify any of the following
or any combination of the following shall submit an application for a sewer
connection permit to the department:
(1) Any
extension of an interceptor sewer, whether public or private, regardless of
flow;
(2) Any
wastewater connection or other discharge in excess of 5,000 gallons per day
(gpd);
(3) Any
wastewater connection or other discharge to a WWTP operating in excess of 80 percent design flow capacity or design loading capacity
based on actual average flow or loadings for 3 consecutive months;
(4) Any sewage
pumping station greater than 50 gpm or serving more
than one building; or
(5) Any
proposed sewer that serves more than one building.
(b) The applicant for a sewer connection permit
shall provide the following to the department:
(1) Complete
and submit electronically the "Sewer Connection Permit Application",
NHDES-W-09-004, May 2025, available at https://onlineforms.nh.gov/?formtag=NHDES-W-09-008;
(2) All
applicable engineering documents required by Env-Wq 703.01 through Env-Wq
703.05;
(3) The
signature of and
a statement from the engineer of record that the plans and specifications for the
proposed sewer connection are in substantial compliance with requirements of
Env-Wq 700, with the exception of any waiver requests identified in the
application;
(4) A certification from the municipality
providing sewerage collection facilities serving the proposed connection certifying that the municipal sewage collection
system facilities have been demonstrated, pursuant to Env-Wq 703.07(c), to have
adequate processing capability for the proposed added hydraulic flow and
organic load at the time of connection and that the proposed sewer connection or
sewerage design meet with the approval of the local jurisdictional authority;
(5) A certification from the
municipality providing wastewater treatment facilities serving the proposed
connection certifying that the municipal wastewater treatment system facilities
have been demonstrated, pursuant to Env-Wq 703.07(c), to have adequate
processing capability for the proposed added hydraulic flow and organic load at
the time of connection;
(6) The name, title, and
signature of each municipality official who is authorized to sign on behalf of
the municipality; and
(7) The application fee in
the amount specified in RSA 485-A:4, IX-a, as reprinted in Appendix C.
(c) The department shall issue a sewer connection
permit or permit extension only if the receiving WWTP and the receiving sewerage are, or will be, capable of adequately processing
the added hydraulic flow and organic load at the time of connection.
(d) A sewer connection permit shall be valid for
3 years from the date of issuance.
(e) Upon written request by a permittee, the
department shall grant a maximum of one permit extension for 2 years from the
date of issuance, if the receiving WWTP and the receiving sewerage
are, or will be, capable of adequately processing the added hydraulic flow and
organic load at the time of connection.
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Env-Wq 703.08 Project Revision and Approval Requirements.
(a) For projects that receive any state or
federal funds, the owner shall obtain written approval of the design plans and
specifications from the department prior to bidding the project.
(b) For all other projects, the owner shall:
(1) Submit the
design plans and specifications at least 30 days prior to the anticipated start
of construction, as per RSA 485-A:4, VI; and
(2) Obtain
written approval of such plans and specifications prior to commencing
construction.
(c) No deviations from approved plans or
specifications shall be made without prior written approval from the department
in accordance with this chapter. All
deviations from the original approved plans or specifications shall be
reflected in the record drawings.
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Env-Wq 703.09 Contract and Bidding Requirements. Owners of projects that might receive state
or federal funds shall comply with all applicable requirements of Env-Wq 500.
Source. (See Revision Note at chapter heading for
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PART Env-Wq 704
DESIGN OF SEWERAGE
Env-Wq 704.01 Type
of Sewerage.
(a) All new sewerage and extensions of existing
sewerage shall be designed as separated sanitary and
storm systems.
(b) Rain water from roofs, streets, and other
paved areas, and groundwater from foundation drains, geothermal systems, and
sump pumps shall be excluded from the sanitary sewer.
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Env-Wq 704.02 Design
Period.
(a) Sewerage pipes, sewerage structures, and pumping
facility
structures shall
be designed to accommodate flows anticipated for the projected 50-year
build-out of the project service area.
(b) Sewerage pumping equipment shall be designed to
accommodate flows anticipated for the projected 20-year build-out of the
project service area.
(c) Anticipated flows shall be calculated using
population projections based on historical population data from the United
States Census Bureau for no less than 20 years prior to filing the application.
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Env-Wq 704.03 Design
Flow Basis.
(a) Sanitary waste flows from residentially-,
commercially-, or industrially-zoned areas shall be measured.
(b) For proposed facilities, sanitary waste flows
shall be estimated on the basis of the following:
(1) For
commercial areas, recreational facilities, or industrial parks, as specified in
Tables 3-3, 3-4, and 3-5 of Metcalf and Eddy/AECOM, “Wastewater Engineering
Treatment and Resource Recovery”, 5th edition, available as noted in Appendix
B, unless design for a lower flow can be justified based on actual flow records
or implementation of water conservation measures; and
(2) For
residential areas, an average daily per capita flow as specified in Table 3-2
of Metcalf and Eddy/AECOM, “Wastewater Engineering: Treatment and Resource
Recovery”, 5th edition, available as noted in Appendix B, unless design for a
lower flow can be justified based on actual flow records or implementation of
water conservation measures.
(c) New sewerage shall be designed to carry the
peak hourly flow rate, calculated as the product of the average daily flow rate
for the service area multiplied by a peaking factor. For gravity sewers, an infiltration allowance
shall be added in accordance with (f), below.
(d) Peaking factors for average daily flow rates
in excess of 100,000 gpd shall be as derived from Figure 2.1 of TR-16, “Guides
for the Design of Wastewater Treatment Works”, by the New England Interstate
Water Pollution Control Commission, revised 2016 Edition, available as noted in
Appendix B. A peaking factor of 6 shall
be used for average daily flows less than 100,000 gpd.
(e) Design of interceptor sewers shall be based
on the greater of the estimated future peak contributory flow from the
collection system served or 2.5 times the estimated future average daily flow
of the tributary system.
(f) Infiltration allowance for the design of
gravity sewers shall be as follows:
(1) For areas
to be sewered in the future, an infiltration allowance of 150 gpd per acre
shall be used;
(2) For sewers
under design, an allowance of 300 gallons per inch diameter per mile per day
shall be made; or
(3) For sewers
in use as of March 25, 2006 intended to be connected
by the interceptor sewer under design, infiltration shall be measured during
high spring groundwater conditions.
Source. (See Revision Note at chapter heading for
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Env-Wq 704.04
Details of Design and Construction of Gravity Sewers.
(a) A gravity sewer may be smaller than 8 inches
in nominal diameter only if the sewer:
(1) Is
constructed on a dead-end or cul-de-sac street;
(2) Serves, or
is planned to serve, no more than 10 residences;
(3) Has a total
estimated flow no greater than 2,000 gpd; and
(4) Has a
nominal diameter of 6 inches and a minimum pipe slope of 0.01 feet per foot.
(b) Sewers shall be buried to a minimum depth of
6 feet below grade in all roadway locations and to a minimum depth of 4 feet
below grade in all cross-country locations.
(c) Sewer pipe diameter shall be
determined using the following methodology:
(1) New sewers up to 15
inches in diameter shall be designed to flow half full;
(2) New
sewers larger than 15 inches shall be designed to flow three-fourths full; or
(3) An engineering
analysis that considers current and future design flow information and provides
commensurate reserve capacity in the sewer.
(d) Sewers shall be designed and constructed at
such slopes as to prevent deposition of solids, with a minimum flow velocity
for design purposes of 2 feet per second when flowing full.
(e) The minimum
allowable slope shall be as set forth in Table 704-1, below:
Table 704-1
Minimum Pipe Slope
|
Nominal Pipe
Diameter (Inches) |
Minimum Slope (feet/foot) |
|
8 |
0.0040 |
|
10 |
0.0028 |
|
12 |
0.0022 |
|
14 |
0.0017 |
|
15 |
0.0015 |
|
16 |
0.0014 |
|
18 |
0.0012 |
|
21 |
0.0010 |
|
24 |
0.0008 |
|
27 |
0.0007 |
|
30 |
0.0006 |
|
36 |
0.0005 |
|
42 |
0.0004 |
|
48 and larger |
0.0003 |
(f) The slope
requirements set forth in (e), above, shall not be met by using sewers that are larger than
required based on design flow calculations.
(g) Sewers smaller
than 48 inches in nominal diameter shall be laid with straight alignment
between manholes.
(h) When a smaller sewer joins a larger one, the
invert of the larger sewer shall be lowered sufficiently to maintain the same
hydraulic gradient. An approximate
method which may be used for securing these results is to place the 0.8 depth
point of both sewers at the same elevation.
(i) A reduction in
the size of the outgoing sewer from a manhole shall be allowed only on sewers
larger than 24-inch diameter and only if the capacity of the outgoing
sewer is not exceeded.
(j) Where velocities greater than 10 feet per
second are anticipated, the design shall incorporate measures to protect against pipe abrasion,
displacement, and potential effects of hydraulic jumps. Velocities shall be calculated based on the
peak hourly flow and hydraulic elements related to the depth of flow.
(k) Sewers on 15 percent slopes or greater shall
be securely anchored.
(l) Sewers
crossing streams or located within 10 feet of a stream embankment shall be
protected against erosion.
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Env-Wq 704.05
Gravity Sewer Construction Materials. The technical specifications shall
specify the approved gravity sewer pipe and materials to be used on the
project, as follows:
(a) Ductile iron pipe and fittings shall be
certified by the manufacturer(s) as conforming to the following standards of
the American Water Works Association (AWWA):
(1) AWWA C151/A21.51-23 for
ductile iron pipe, centrifugally cast in metal- or sand-lined molds, for water,
wastewater, and reclaimed water systems, available as noted in Appendix B; and
(2) AWWA C150/A21.50-21(R23)
for thickness design of ductile iron pipe and with ASTM A536-24 for
ductile iron castings, available as noted in Appendix B;
(b) Joints shall
be mechanical type, push-on type, or ball-and-socket type as appropriate for
the specific application;
(c) Plastic
gravity sewer pipe and fittings shall be certified by the manufacturer as
complying with the standards listed in Table 704-2, below:
Table 704-2
Plastic Pipe
|
ASTM Standard |
Generic Pipe
Material |
Sizes Approved |
|
D3034-24 |
Polyvinyl chloride (PVC), solid wall |
All
diameters |
|
F794-21 |
PVC, profile, dual-walled corrugated |
4-inch through 48-inch |
|
F1760-16R20 |
PVC, recycled, non-pressure |
All diameters |
(d) Plastic sewer
pipe shall have a pipe stiffness rating of at least 46 pounds per square inch
at 5 percent pipe diameter deflection, as measured by the manufacturer in
accordance with the ASTM D2412-21 standard, available as noted in Appendix B;
(e) Joint seals for PVC pipe shall be oil
resistant compression rings of elastomeric material and certified by the
manufacturer as conforming to the ASTM D3212-21 standard, available as noted in Appendix B, and
shall be push-on, bell-and-spigot type;
(f) Concrete pipe
shall be certified by the manufacturer as conforming to the AWWA C302-22
standard,
available as noted in Appendix B;
(g) Pre-stressed
concrete cylinder pipe and fittings shall be certified by the manufacturer as
conforming to the AWWA C301-14(R19) standard, available as noted in Appendix B; and
(h) Joints for concrete
cylinder pipe shall be made of oil resistant elastomeric material and certified
by the manufacturer as conforming to the AWWA C301-14(R19) standard, available as
noted in Appendix B.
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Env-Wq 704.06
Gravity Sewer Pipe Testing.
(a) All new gravity sewers shall be tested for
water tightness by the use of low-pressure air tests.
(b) Low-pressure air testing shall be in
conformance with the following testing standards:
(1) ASTM F1417-11a (2024)
“Standard Practice
for Installation Acceptance of Plastic Non-Pressure Sewer Lines Using Low-Pressure
Air”, available as noted in Appendix B; or
(2) Uni-Bell
PVC Pipe Association Uni-B-6-98, “Recommended Practice for Low-Pressure Air Testing of Installed
Sewer Pipe”, available as noted in Appendix B.
(c) All new gravity sewers shall be:
(1) Cleaned and
visually inspected using a lamp test and by introducing water to determine that
there is no standing water in the sewer; and
(2) True to
line and grade following installation and prior to use.
(d) All plastic sewer pipe shall be visually
inspected and deflection tested not less than 30 days nor more than 90 days
following installation.
(e) The maximum allowable deflection of flexible
sewer pipe shall be 5% percent of average inside diameter. A rigid ball or mandrel with a diameter of at
least 95% of the average inside pipe diameter shall be used for testing pipe
deflection. The deflection test shall be conducted without mechanical pulling
devices.
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Env-Wq
704.07 Details of Design and
Construction of Force Mains.
(a) Force mains shall be sized to yield a
cleansing velocity of 3 feet per second or greater at design pumping rate.
(b) Force mains shall be 4 inches or larger in
nominal diameter except when used in conjunction with grinder pumps and necessary
to achieve adequate cleansing velocity at design pumping rate.
(c) To prevent air locking, force mains shall be
provided with an automatic air relief valve at each high point, installed
within a manhole structure that meets the design requirements of Env-Wq 704.12
through Env-Wq 704.17.
(d) Force mains shall enter the gravity sewer
system at the flow line of the receiving manhole.
(e) Force mains shall be provided with a drainage
blow-off at each low point that:
(1) Has a
properly valved connection for a vacuum truck or other suitable containment
device; and
(2) Is
installed within a manhole structure that meets the design requirements of
Env-Wq 704.12 through Env-Wq 704.17, with sufficient space for handling the
displaced waste without danger of pollution or health hazard.
(f) Force mains pipe joints shall include mechanical joint
restraint or thrust blocks made from inorganic, corrosion-resistant
material at all bends, elbows, tees, and junctions. Heat fused high density polyethylene joints do not
require mechanical restraint or thrust blocking.
(g) Force mains shall be designed to withstand
instantaneous hydrostatic pressures of at least 2.5 times the design total
dynamic head or at least 100 psi, whichever is greater.
Source. (See Revision Note at chapter heading for
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Env-Wq 704.08 Force Main Construction Materials.
(a) Force mains shall be constructed of ductile
iron (DI), high density polyethylene (HDPE), or PVC material.
(b) Force mains shall be treated as gravity
sewers for purposes of foundation bedding and backfill requirements.
(c) PVC pipe used for force mains shall be
certified by its manufacturer as conforming to the ASTM D2241-24 or ASTM
D1785-21a
standards,
available as noted in Appendix B.
(d) HDPE pipe used for force mains shall be
certified by its manufacturer as conforming to the ASTM D3035-22 or ASTM
F714-24 standards, available as noted in Appendix B.
(e) If DI pipe is used in an environment that
could cause corrosion or other deterioration of or damage to an iron pipe, or
otherwise reduce the typical life expectancy of the pipe, such as might occur
with certain soil types, low pH levels, or water conditions, the pipe shall be
protected against corrosion, such as with cathodic protection.
Source. (See Revision Note at chapter heading for
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Env-Wq 704.09 Force Main Testing. Force mains shall be tested in
accordance with AWWA C600-23, “Installation of Ductile-Iron Mains and Their Appurtenances”
standard, available as noted in Appendix B, at a pressure equal to the greater
of 150 percent of the design operating total dynamic head or at least 100 psi.
Source. (See Revision Note at chapter heading for
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Env-Wq 704.10 Pressure Sewer Systems.
(a) A pressure sewer system shall have at least
one grinder pump at each building or residence that is connected to the system.
(b) The minimum capacity requirements for a
pressure sewer system and each grinder pump connected to a pressure sewer
system shall be determined based on hydraulic modeling of the entire pressure
sewer system and the main sewer to which the pressure sewer is proposed to be
connected.
(c) A design report
for a pressure sewer system shall be prepared by the engineer and submitted in
accordance with Env-Wq 703.01.
(d) Pressure sewer design shall provide a minimum cleansing
velocity of 2 feet per second.
(e) Pressure sewers shall be constructed with force main
materials as specified in Env-Wq 704.08 and tested as specified in Env-Wq
704.09.
(f) Grinder pumps for pressure sewer systems
shall be:
(1) Wet well
type;
(2) Readily
removable without manual disconnection of piping;
(3) Rotating
type with a stationary hardened and ground stainless steel shredding ring with
stainless steel cutters;
(4) Capable of
reducing all components in typical domestic sewage, including a reasonable
number of foreign objects, including but not limited to wood, paper, plastic,
glass, and rubber, to a size that will pass through pump passages and a
1.25-inch nominal diameter pipe;
(5) Positioned
so solids are fed into pump from the bottom in an upward flow;
(6) Capable of
processing foreign objects without jamming, stalling, or overloading;
(7) Accessible
for maintenance and replacement; and
(8) Equipped
with:
a. Non-fouling
sensing devices for high level alarms;
b. A visible
alarm light;
c. An audible
alarm;
d. A
gravity-operated, integral anti-siphon valve with corrosion-resistant moving
parts; and
e. A suitable
receptacle and transfer switch in the electric supply panel for connection to a
portable generator.
(g) A grinder pump tank shall be designed to
withstand HS-20 loading if installed in a location where traffic loads are
anticipated and consist of:
(1) A manhole
meeting the requirements of Env-Wq 704.12 through Env-Wq 704.17;
(2) A
reinforced concrete tank;
(3) A high
density polyethylene tank; or
(4) A
fiberglass-reinforced polyester resin using a filament wound process, layup, and spray
technique.
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Env-Wq 704.11 Trench
Construction.
(a) Pipe trench bedding material for excavation
below grade shall be screened gravel or crushed stone meeting the ASTM C33/C33M-24a stone
size No. 67 standard, available as noted in Appendix B.
(b) Subject to (c), below, the pipe sand blanket
material shall be graded sand free from organic materials, graded such that 100
percent passes a ½-inch sieve and a maximum of 15 percent passes a #200 sieve.
(c) In lieu of the sand blanket specified in (b),
above, a stone envelope 6 inches thick completely around the pipe using ¾-inch
stone may be used.
(d) Pipe bedding material shall extend from a
horizontal plane through the pipe axis to 6 inches below the bottom of the
outside surface of the pipe.
(e) Pipe sand blanket material shall cover the
pipe a minimum of 12 inches above the crown of the outside surface.
(f) Compaction shall be in 12-inch layers for
bedding and blanket materials.
(g) Backfill material shall be compacted in no
more than 3-foot thick layers to the ground surface except for road
construction where the final 3 feet shall be compacted in no more than 12-inch
thick layers to the road base surface.
(h) Trench backfill material in roadway locations
shall be natural materials excavated from the trench during construction,
excluding:
(1) Debris;
(2) Pieces of
pavement;
(3) Organic
matter;
(4) Top soil;
(5) Wet or soft
muck;
(6) Peat or
clay;
(7) Excavated
ledge material;
(8) Rocks over
6 inches in the largest dimension; and
(9) Any
material not approved by the engineer.
(i) Trench backfill
at cross-country locations shall be as described in (h), above, except that top
soil, loam, muck, or peat may be used provided the completed construction will
be stable, and provided that access to the sewer for maintenance and
reconstruction is preserved.
(j) Backfill shall be mounded 6 inches above
original ground at cross country locations.
(k) Base course for trench repair shall meet the
requirements of Division 300 of the “Standard
Specifications for Road and Bridge Construction” of the New Hampshire
department of transportation, available as noted in Appendix B.
(l) Where sheeting is placed alongside the pipe
and extends below mid-diameter, the sheeting shall be cut off and left in place
to an elevation not less than one foot above the top of the pipe and at least 3
feet below finished grade.
(m) Trenches for sewer pipes with slopes over
0.08 feet per foot, trenches for sewer pipes below seasonal high ground water
level, and trenches for sewer pipes downstream of and within the hydraulic
influence of waterways or wetlands shall have impervious trench dams
constructed every 300 feet to prevent potential disturbance to pipe bedding and
blanket materials.
(n) Precautions shall be taken to avoid
groundwater pooling at the surface by providing drainage to a suitable outlet
at catch basins or run-off swales.
(o) For trenches for sewer pipes in ledge,
excavation shall extend to at least 12 inches below the bottom of the sewer
pipe.
(p) All sewers shall be marked using
metal-impregnated marking tape or tracer wire that can be located using metal
detection equipment.
Source. (See Revision Note at chapter heading for
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Env-Wq 704.12 Manholes:
General Construction Requirements.
(a) All component parts of manhole structures
shall have the strength, leak resistance, and space necessary for the intended
service.
(b) Manhole structures shall be designed to
withstand HS-20 loading and shall not leak in excess of one gpd per vertical
foot of manhole for the life of the structure.
(c) Barrels, cone sections, and concrete grade
rings shall be constructed of precast reinforced concrete.
(d) Base sections shall be of monolithic
construction to a point at least 6 inches above the crown of the incoming pipe.
(e) Horizontal joints between sections of precast
concrete barrels shall be of an overlapping type, sealed for water-tightness
using a double row of an elastomeric or mastic-like sealant.
(f) Pipe to manhole joints shall be as follows:
(1)
Elastomeric, rubber sleeve with watertight joints at the manhole opening
and pipe surfaces;
(2) Cast into
the wall or secured with stainless steel clamps;
(3) Elastomeric
sealing ring cast in the manhole opening with seal formed on the surface of the
pipe by compression of the ring; and
(4) Non-shrink
grouted joints where watertight bonding to the manhole and pipe can be
obtained.
(g) Manhole cone sections shall be eccentric in
shape.
(h) All precast sections and bases shall have the
date of manufacture and the name or trademark of the manufacturer impressed or
indelibly marked on the inside wall.
(i) All precast sections and bases shall be
coated on the exterior with a bituminous damp-proofing coating.
(j) Manholes that are not replacing existing
manholes shall have a brick paved shelf and invert constructed to conform to
the size of pipe and flow. At changes in
direction, the inverts shall be laid out in curves of the longest radius
possible tangent to the center line of the sewer pipes. Shelves shall be constructed to the elevation
of the highest pipe crown and sloped to drain toward the flowing through
channel. Underlayment of invert and
shelf shall consist of brick masonry.
Inverts and shelves shall be placed after testing of the manhole.
(k) Replacement manholes where there is an
established line and grade through which the sewer enters and exits the manhole
shall have:
(1) A brick
paved shelf and invert constructed to conform to the size of pipe and flow as
required in (j) above;
(2) A precast
concrete shelf and invert with the shelf constructed to the elevation of the
highest pipe crown and sloped to drain toward the flowing through channel; or
(3) A
fiberglass insert with the shelf constructed to the elevation of the highest
pipe crown and sloped to drain toward the flowing through channel.
(l) When manhole depth is less than 6 feet, a
reinforced concrete slab cover may be used in lieu of a cone section, provided
the slab has an eccentric entrance opening and be capable of supporting HS-20
loads.
(m) The minimum internal diameter of manholes
shall be 48 inches. For sewers larger
than 24-inch diameter, manhole diameters shall be increased so as to provide at
least 12 inches of shelf on each side of the sewer.
(n) In the flow channel, a drop of at least 0.1
feet shall be provided between incoming and outgoing sewers on all manholes.
(o) Slope across manholes shall be the average
slope of the incoming and outgoing sewers.
Design shall include measures to prevent hydraulic jumps across the
manholes.
(p) Watertight manhole covers shall be used for
all manholes located in flood-prone areas as determined by the municipality.
(q) Electrical equipment installed or used in
manholes shall conform to the National Electric Code (NEC) adopted by reference
in the state building code pursuant to RSA 155-A:1, IV, for installation in
areas classified by the NEC as Class 1, Division 1.
(r) Precast bases shall be placed on a 6-inch
layer of compacted bedding material that conforms to the ASTM C33/C33M-24a No. 67
stone standard, available as noted in Appendix B. The excavation shall be dewatered while
placing bedding material and setting the base or pouring concrete.
Source. (See Revision Note at chapter heading for
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Env-Wq
704.13 Manholes: Materials of Construction.
(a) Materials of construction for manholes shall
be as follows:
(1) Concrete
for manholes and concrete grade rings shall conform to the requirements for
class AA concrete in the New Hampshire department of transportation’s “Standard Specifications for Road and
Bridge Construction”, available as noted in Appendix B;
(2) Reinforcing for concrete manholes and
concrete grade rings shall be steel or structural fibers that conform to the New
Hampshire department of transportation’s “Standard
Specifications for Road and Bridge Construction”, available as noted in Appendix B;
(3) Precast
concrete barrel sections, cones, and bases shall be certified by their
manufacturer(s) as conforming to the ASTM C478/C478M-22 standard, available as
noted in Appendix B;
(4) The manhole
frame and cover shall provide a 30-inch diameter clear opening;
(5) The manhole
cover shall have the word “SEWER” in 3-inch letters cast into the top surface;
(6) The
castings shall be of even-grained cast iron, smooth, and free from scale,
lumps, blisters, sand holes, and defects;
(7) Contact
surfaces of covers and frames shall be machined at the foundry to prevent
rocking of covers in any orientation;
(8) Castings
shall be equal to class 30 and certified by their manufacturer as conforming to
the ASTM A48/48M-22 standard, available as noted in Appendix B; and
(9) Brick
masonry for shelf, invert, and grade adjustment shall be certified by its
manufacturer as complying with the ASTM C32-23 standard, available as noted in Appendix B,
clay or shale, for grade SS hard brick, with no more than 5 layers of brick for
grade adjustment.
(b) Materials of construction for manhole grade
adjustment shall be as follows:
(1) Grade
adjustment rings shall be constructed with either Grade SS hard brick that has
been certified by its manufacturer as meeting the ASTM C32-23
standard,
available as noted in Appendix B or reinforced concrete meeting the
requirements of this section; and
(2) Grade
adjustment rings shall:
a. Be sized to
the opening of the manhole; and
b. Not obstruct
the access to the manhole.
(c) Mortar used in manhole construction shall
comply with the following:
(1) Mortar
shall be composed of Type II Portland cement and sand with or without hydrated
lime addition;
(2) Proportions
in mortar of parts by volumes shall be as shown in table 704-4:
Table 704-4: Proportions of Cement, Sand, and Hydrated
Lime
|
Hydrated Lime |
Sand |
Type II
Portland Cement |
|
None |
4.5 parts |
1.5 parts |
|
0.5 part |
4.5 parts |
one part |
(3) Cement
shall be type II Portland cement that is certified by its manufacturer as
conforming to the ASTM C150/C150M-24 standard, available as noted in Appendix B;
(4) Hydrated
lime shall be type S that is certified by its manufacturer as conforming to the
ASTM C207-24
standard,
available as noted in Appendix B;
(5) Sand shall
consist of inert natural sand that is certified by its supplier as conforming
to the ASTM C33/C33M-24a
standard,
available as noted in Appendix B; and
(6) Concrete for drop supports shall conform to
the requirement for class AAA concrete of the New Hampshire
department of transportation’s “Standard Specifications for Road and Bridge
Construction” available as noted in Appendix B.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq
704.14 Manholes: Steps.
Manhole steps shall:
(a) Be permitted only at the request of the
system owner;
(b) Be manufactured of stainless steel,
plastic-covered steel, or plastic;
(c) Be shaped so that they cannot be pulled out
of the concrete wall into which they are secured;
(d) Be certified by the manufacturer as meeting
the ASTM C478/C478M-22
standard for load carrying capacity and pull-out resistance, available as noted
in Appendix B;
(e) Not be secured with mortar;
(f) Be approximately 14 inches by 10 inches in
dimension;
(g) Have a drop section or raised abutments to
prevent sideways slippage off the step; and
(h) Have non-skid safety serrations on the foot
contact surfaces.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
704.15 Manholes: Placement. Manholes shall be located as follows:
(a) Manholes shall be installed at the end of
each gravity sewer, force main, and pressure sewer, at all intersections, and
at all changes in grade, size, or alignment; and
(b) For gravity sewers only, in establishing a
maximum space between manholes, the engineer shall not exceed the distance that
can be cleaned by the cleaning equipment the owner already has on hand or
proposes to obtain. In no case shall the
distance between manholes be greater than the distances shown below in Table
704-5:
Table 704-5: Manhole Spacing Requirements
|
Sewer Diameter, inches |
Maximum Distance between Manholes, feet |
|
15 or less |
400 |
|
18-30 |
500 |
|
36-48 |
600 |
|
>48 |
1,000 |
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq
704.16 Manholes: Drop Entry Construction Requirements.
(a) The invert of the incoming pipe shall be no
more than 6 inches above the invert of the outgoing pipe unless a drop entry
pipe is used.
(b) Sewer slopes shall be adjusted to avoid
differences in incoming and outgoing pipe inverts greater than 6 inches unless
a drop entry pipe is used. Invert
differences greater than 6 inches and less than 24 inches shall be eliminated
by adjusting the sewer slope.
(c) A drop entry pipe shall be provided for any
sewer entering a manhole at an elevation of 24 inches or more above the manhole
invert. The drop pipe may be constructed
internal or external to the manhole.
(d) The maximum size limits and number of
internal drop pipes within a manhole shall be as shown in Table 704-6, below:
Table 704-6: Size Limits and Number Requirements for
Internal Drop Pipes
|
Manhole Diameter |
Internal Drop Pipe Size |
Number of Pipes Required |
|
4-foot, 0-inch |
8-inch or 10-inch |
1 |
|
5-foot, 0-inch |
15-inch |
1 |
|
8-inch or 10-inch |
2 |
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 704.17 Manholes: Testing.
(a) Manholes shall be tested for leakage using a
vacuum test in accordance with the ASTM C1244/C1244M-20 standard, available as noted
in Appendix B. A manhole may be
backfilled prior to performing a vacuum test, but if the manhole fails the
vacuum test, backfill shall be removed so repairs to the manhole can be made
from the outside of the manhole prior to retesting.
(b) The manhole vacuum test shall conform to the
following:
(1) The initial
vacuum gauge test pressure shall be 10 inches Hg; and
(2) The minimum
acceptable test hold time for a 1-inch Hg pressure drop to 9 inches Hg shall
be:
a. Not less
than 2 minutes for manholes less than 10 feet deep in depth;
b. Not less
than 2.5 minutes for manholes 10 to 15 feet deep; and
c. Not less
than 3 minutes for manholes more than 15 feet deep.
(c) The manhole shall be repaired and retested if
the test hold times fail to achieve the acceptance limits specified in (b),
above.
(d) Inverts and shelves shall not be installed
until after successful testing is completed.
(e) Immediately following completion of the
leakage test, the frame and cover shall be placed on the top of the manhole or
some other means used to prevent accidental entry by unauthorized persons,
children, or animals, until the contractor is ready to make final adjustment to
grade.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 704.18
Inverted Siphons.
(a) Inverted siphons shall have not less than 2
barrels with a minimum pipe size of 6 inches.
(b) Maintenance manholes and appurtenances shall
be provided at both ends of the siphon to facilitate convenient flushing and
maintenance of the siphons.
(c) Pipe sizes and a hydraulic head shall be
selected to secure velocities of at least 3.0 feet per second for average
design flows in each siphon.
(d) The inlet and outlet details shall be
arranged so that flow can be diverted to one barrel, so that either barrel may
be taken out of service.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 704.19 Protection
of Water Supplies.
(a) There shall be no physical connection between
a public or private potable water supply system and any sewerage such that
sewage or polluted water could pass into the potable supply. No water pipe shall pass through or come in
contact with any part of any sewer or sewer manhole.
(b) No sewer shall be located within the
applicable well protective radii established in Env-Dw 300 for any public water
supply well or within 75 feet of any private water supply well.
(c) Sewers shall be located at least 10 feet
horizontally from any existing or proposed water main.
(d) A deviation from the separation requirements
of (b) or (c), above, shall be allowed where necessary to avoid conflict with
subsurface structures, utility chambers, and building foundations, provided
that the sewer is constructed with force main construction materials that meet
the requirements in Env-Wq 704.08.
(e) Whenever sewers must cross water mains, the
sewer shall be constructed as follows:
(1) Vertical
separation of the sewer and water main shall be not less than 18 inches, with
water above sewer; and
(2) Sewer pipe
joints shall be located at least 6 feet horizontally from the water main.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 704.20 Service
Connections.
(a) Service connections shall use sanitary tee or
wye fittings for all new sewer construction.
(b) The centerline of all building connections
shall enter the top half of the sewer.
(c) Any service connection with a vertical rise
up to 4 feet may have the sewer fitting set vertically.
(d) Any service connection with a vertical rise
up to 12 feet shall employ non-encased risers that protect against pipe
penetration or failure at the fitting by the use of bell-on-bell connections.
(e) For existing sewers where fittings cannot be
installed, saddle connections shall be used.
(f) Pressure sewerage shall have an isolation and check
valve
assembly installed on each service lateral at the property line. The assembly shall
consist of a check valve, a curb stop valve, and a curb box.
(g) Roof downspouts, exterior or interior
foundation drains, sump pumps, or other sources of surface water run-off or
groundwater shall not be directly or indirectly connected to a public sewer.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 705
SEWAGE PUMPING STATIONS
Env-Wq 705.01 Sewage Pumping Station Design Requirements: General.
(a) Sewage pumping stations shall be protected
against flooding in accordance with Env-Wq 706.03(a), (b), and (d).
(b) Flood elevations shall be determined in
accordance with Env-Wq 706.03(e) and (f).
(c) Each sewage pumping station shall be
protected against extreme weather conditions, such as excessive heat or
humidity or excessively cold temperatures, that could cause the pump station
components to stop functioning.
(d) Sewage pumping stations and all ancillary
equipment shall be accessible to personnel and service vehicles.
(e) Sewage pumping stations shall be designed to:
(1) Minimize
energy consumption and lifecycle costs;
(2) Prevent
surcharging of the sewage collection system during design conditions; and
(3) Prevent
unauthorized discharge of raw sewage.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 705.02 Sewage Pumping
Station Design Requirements: Wet Well
and Dry Well Construction.
(a) The wet well and the discharge manifold shall
be configured to prevent grit from settling back into pump discharge lines of
pumps that are not operating.
(b) Wet and dry wells including their
superstructure shall be completely separated and sealed.
(c) Wet well designs shall avoid vortexing and air entrainment near the pump suction
intakes.
(d) A separate sump pump shall be provided in the
dry well to remove leakage or drainage, with the discharge above the alarm
level of the wet well.
(e) Wet wells for sewage pumping stations of
greater than 200 gpm capacity shall have either:
(1) Division
walls so that the station can be kept in operation when work is required in the
wet well; or
(2) A bypass
connection to allow for connection of a pump around the wet well for
maintenance, repairs, and construction.
(f) With the exception of sewage pumping stations subject
to Env-Wq 705.03(n), the effective volume of the wet well shall be sized considering:
(1) A filling time of 30
minutes or less under design average daily flow rates;
(2) The pump type, motor size,
and allowable frequency of starts per hour as follows:
a. For dry well
motors, a maximum of 6 starts per hour for motors 25 hp and smaller, 4 starts
per hour for motors between 33 and 100 hp and 2 starts per hour for motors
between 135 and 270 hp; and
b. For
submersible pumps that have motors designed to operate in liquid, a maximum of
10 starts per hour for motors less than 50 hp, 6 starts per hour for motors
between 50 and 100 hp and 4 starts per hour for motors larger than 100 hp; and
(3) Provisions to limit the
filling time under initial operating conditions to not exceed 30 minutes when
the initial anticipated tributary sewage flows are significantly less than the
design flows.
(g) The wet well floor shall have a minimum slope
of 1 to 1 to the hopper bottom.
(h) The horizontal area of the hopper bottom
shall be limited to that area required for proper installation and function of
the inlet.
(i) Wet wells shall be designed to be watertight and gas tight.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 705.03 Sewage Pumping Station Design
Requirements: Allowable Pump Types, Pump
Controls, and Pump Size.
(a) The following types of sewage pumping
stations shall be allowed:
(1) Dry well or
wet well type designs with pumps and drives located in a separate dry chamber
with flooded suctions;
(2) Suction
lift type with pumps and drives in a separate dry chamber; and
(3) Submersible
type with pumps submerged.
(b) A minimum of 2 pumps, each designed to handle
peak hourly flows, shall be provided.
(c) Where 3 or more pumps are provided, they
shall be designed such that, with any one unit out of service, the remaining
units shall have the capacity to handle peak hourly sewage flows.
(d) The use of jockey pumps shall be evaluated to
optimize the efficiency of the pumping station operation.
(e) All pumps shall be protected from damage due
to large solid objects.
(f) Sewage pumps, with the exception of grinder
pumps, shall be capable of passing a 3-inch sphere. Pumps preceded by a grinder
unit shall be capable of passing a 2.5-inch sphere.
(g) Submersible pumps shall be capable of removal
without disconnecting pipes or dewatering and reseating using non-corroding
guide rails or cables.
(h) Self-priming suction lift pump systems shall
be designed such that:
(1) The
system’s reprime capacity is greater than the static suction head; and
(2) The
system’s available net positive suction head is at least 6 feet greater than
the required net positive suction head.
(i) Pumps shall be
protected by check valves from being driven in the reverse direction.
(j) Pump controls shall provide autostart of lag pump should lead pump fail to start.
(k) Flooded suction pumping systems shall be
designed such that:
(1) Shut-off
valves are provided in the suction piping;
(2) Shut-off
valves and check valves are provided in the discharge piping; and
(3) Discharge
shut-off valves are located downstream of the check valve.
(l) Shut-off and check valves for submersible
pumps shall be placed in a separate chamber for ease of maintenance.
(m) Individual grinder pumps part of a pressure sewer system
designed in accordance with Env-Wq 704.10 shall not be subject to the
requirements of this subchapter.
(n)
Low-flow sewage pumping stations with a capacity of
less than 120 gpm shall be grinder type submersible
pumps with wet wells and pump controls designed to minimize wet well storage
time and discourage septic conditions from developing within the sewerage
system.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 705.04 Sewage Pumping Station Design
Requirements: Pump Station Access. Sewage pumping stations shall meet the
following requirements:
(a) Dry wells shall provide accessibility for the
repair and removal of pumps, motors, and other items of equipment that are
essential to the sewage pumping process;
(b) Separate exterior entrances shall be provided
to both wet wells and dry wells of sewage pumping stations;
(c) Vertical distances between floors or rest
landings shall not exceed 12 feet;
(d) Safety barriers to prevent falling shall be
provided at landings;
(e) Lifting equipment shall be provided for
submersible pump removal; and
(f) Lifting chains shall be stainless steel or
other corrosion resistant material.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
705.05 Sewage Pumping Station Design
Requirements: Flow and Pump Usage Measurement.
(a) Sewage pumping stations with capacities of
more than 250 gpm or equipped with variable speed
pumps shall have continuous flow recording and totalizer capability.
(b) Sewage pumping stations equipped with
constant speed pumps with capacities of 250 gpm or
less shall have:
(1) A running
meter that indicates the cumulative running time of each pump; or
(2) The
continuous flow recording and totalizer capability as per (a), above.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
705.06 Sewage Pumping Station Design
Requirements: Potable Water Restrictions and Protection.
(a) Where potable water is used for pump sealing
purposes, the potable water supply shall be protected by a break tank or
reduced pressure zone back flow preventer.
(b) Water ejectors connected to a potable water
supply shall be prohibited.
(c) All floor and walkway surfaces shall slope to
a point of discharge.
(d) Connections between raw, partially treated,
or fully treated sewage and potable water shall be prohibited unless adequate
backflow prevention equipment is installed.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 705.07
Sewage Pumping Station Electrical Requirements.
(a) Submersible pumps for sewage pumping stations
shall conform to the NEC requirements adopted by reference in the state
building code pursuant to RSA 155-A:1, IV, for installation in areas classified
by the NEC as class I, division 1.
(b) Electrical systems and components, including
motors, lights, cable, conduits, switch boxes, and control circuits shall be
protected from flooding in accordance with Env-Wq 705.01.
(c) Electrical systems and components including
motors, lights, cable, conduits, switch boxes, and control circuits in enclosed or
partially enclosed spaces where flammable mixtures occasionally might be
present, including raw sewage wet wells, shall be certified by their
manufacturer as:
(1) Complying
with the NEC requirements adopted by reference in the state building code
pursuant to RSA 155-A:1, IV, for class I, division 1 locations; or
(2) Being rated
for class I division 2 requirements where mechanical ventilation is provided in
accordance with the National Fire Protection Association (NFPA) as adopted by
reference in the state fire code in Saf-C 6000 and NFPA 820, available as noted
in Appendix B.
(d) All electrical equipment and work shall
comply with the requirements of NEC as adopted by reference in the state
building code pursuant to RSA 155-A:1, IV, and NFPA as adopted by reference in
the state fire code in Saf-C 6000 and NFPA 820, available as noted in Appendix B.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
705.08 Sewage Pumping Station
Ventilation Requirements.
(a) Mechanical ventilation for personnel and
equipment shall be provided for all occupied spaces within sewage pumping
stations in accordance with the NFPA as incorporated by reference in the state
fire code in Saf-C 6000 and NFPA 820, available as noted in Appendix B.
(b) Mechanical ventilation for below-grade dry
wells shall be provided, and so arranged as to independently ventilate the dry well and
the wet well.
(c) There shall be no interconnection between the
wet well and dry well ventilation systems.
(d) Switches for operation of ventilation
equipment shall be marked and located conveniently.
(e) Dehumidification shall be provided in
below-ground dry wells.
(f) Ventilation of wet wells shall provide at
least 30 air changes per hour if the ventilation system is operated
intermittently, or at least 12 air changes per hour if the ventilation system
is operated continuously.
(g) Fans installed within the wet well structure
shall be suitable for a class I, division 1, group C and D environment.
(h) Ventilation of submersible pump chambers or
suction lift wet wells where there is no occupancy for regular maintenance
purposes may be by gravity ventilation.
(i) Ventilation
exhaust from wet wells shall not cause an odor nuisance to the public or
surrounding occupied buildings.
(j) Access doors to wet wells shall have warning
signs on the underside which read, “Warning - Hazardous Area, enter only with
proper equipment” or “Confined Space, Entry by Permit Only”, as appropriate.
(k) The ventilation system of the dry well shall
be capable of continuously providing at least 6 air changes per hour when the
facility is occupied, and at least 3 air changes per hour when not occupied.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 705.09 Sewage Pumping Station Alarm Systems.
(a) Alarm systems meeting the requirements of (b)
through (j), below, shall be provided for all sewage pumping stations.
(b) The alarm signal shall be activated in any
one of the following circumstances and in any combination of the following
circumstances:
(1) High water
in the wet well;
(2) Low water
in wet well;
(3) Loss of one
or more phases of power supply or severe voltage drop;
(4) High water
level in the pump room sump;
(5) Loss of the
alarm transmission capability;
(6) Standby
generator application, if applicable;
(7) Pump
malfunction, including shaft seal failure;
(8) Loss of air
pressure in a bubbler tube system;
(9) Level
sensing malfunction or failure;
(10) Loss of
ventilation in areas classified as class 1 division 2 and using mechanical
ventilation per the NFPA as incorporated by reference in the state fire code in
Saf-C 6000 and NFPA 820, available as noted in Appendix B;
(11) Intrusion;
or
(12)
Temperature outside normal operating ranges.
(c) The high water and low water alarm triggers
shall be separate devices, independent of the pump wet well level control
system and set at elevations above and below the lag pump on and off
elevations, respectively.
(d) Operation of the alarm system shall be
indicated on a panel with a light which lights up upon activation of the alarm
system.
(e) The power source for the alarm system shall
be:
(1) An
independent battery with continuous charge; or
(2) Main line
power with a back-up battery system, which shall be connected automatically
should main power fail.
(f) The alarm signal shall be transmitted through
a 24 hour per day, 7 day per week notification system to the appropriate
utility operator.
(g) The alarm shall include a local audible
enunciator and a light.
(h) Provision shall be made to permit silencing
of the audible enunciator manually, after the alarm has been sounded, but the
light shall continue until the alarm condition has been rectified.
(i)
Alarm signals for privately-operated
sewage pumping stations shall be transmitted to the responsible maintenance
person directly or via an answering service.
(j) If a central supervisory control and data
acquisition (SCADA) system exists at the WWTP, the pumping station alarms shall
be connected to the SCADA system using programmable logic controller (PLC)
technology.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 705.10 Sewage Pumping Station Operation and Maintenance Manual.
(a) The owner shall have an operation and
maintenance manual that provides information and guidance for day-to-day
operation of each sewage pumping station. The manual shall be readily
accessible, kept up to date, and made available to the department upon request.
(b) The operation and maintenance manual required
by (a), above, shall include all information that is necessary to operate and
maintain the specific equipment at the pumping station, including but not
limited to the following:
(1) Information on
process design assumptions;
(2) Unit
process information that includes detailed process descriptions, control
measures,
and monitoring procedures for processes, if applicable;
(3) Start-up
procedures for each unit operation as applicable and each piece of equipment;
(4) Maintenance
management systems;
(5) Laboratory
test procedures;
(6) Safety
procedures;
(7)
Organizational structure and administrative procedures;
(8)
Troubleshooting procedures;
(9) Emergency
operation plan;
(10) Staffing
requirements;
(11) Process
and instrumentation diagrams;
(12) Checklists
for systems and components for the operator’s use in developing a maintenance
program for pump stations;
(13) Utility
emergency contact information;
(14) Staff
training and licenses necessary for the chief operators and assistant
operators;
(15) A list of
each chemical used at the pump station and what the chemical is used for,
together with the applicable material safety data sheet (MSDS); and
(16) Equipment
supplier manuals.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 705.11 Sewage Pumping Station Emergency Operation.
(a) A sewage pumping station shall be designed to
prevent the back-up, overflow, or other unpermitted discharge of wastewater
from the sewage pumping station during electrical power failures.
(b) An independent engine-generator type source
of electric power shall be provided for electrically-driven pumps. This source shall be automatically activated
by failure of any phase of power supply or upon any fluctuation in voltage, the
amount or duration of which would cause damage to the motors. Installations shall comply with all
applicable requirements of the NEC and the state fire code in Saf-C 6000 and NFPA
820,
available as noted in Appendix B.
(c) The emergency power generator shall be
permanently secured in place, with provisions for removal to facilitate
generator repair or replacement.
(d) Provisions shall be made for automatic and
manual start-up and cut-in. The controls
shall be such that upon automatic start-up under emergency conditions,
shut-down shall be accomplished automatically on restoration of utility power
with controlled shut-down of unit.
Manual shut down shall also be provided.
Provision shall be made to allow pumps to run down before re-energizing
on transfer of power.
(e) The emergency power generator shall be sized
to sequentially start and operate all pumps needed to handle design maximum
waste flows, plus lighting, ventilation, controls, screening, and, if
applicable, grinding.
(f) The emergency power generator shall be
located above grade with ventilation of exhaust gases.
(g) All emergency power generation equipment
shall be provided with instructions for routine exercising, load testing, and
maintenance.
(h) The generator engine controls shall be
equipped with an automatic exerciser which can be set on any selected schedule
to start the generator, run the generator under no-load or load conditions by
selection, and shut the generator off without actuating the alarm system.
(i) Subject to (j),
below, the owner shall provide each emergency generator with enough fuel for
the generator to run under full load or peak station flow for at least 48 hours
or under normal operating conditions for at least 96 hours, whichever requires
the greater amount of fuel.
(j) Alternatives to a permanently installed
emergency power generator may be provided in the following circumstances:
(1) Sewage
pumping stations with capacities of 120 gpm or less
may use wet well storage over and above normal operating system storage
provided that:
a. A suitable
receptacle shall be included in the electrical supply panel for connection to a
portable generator with manual transfer;
b. The storage location of the portable generator or
pumping equipment is identified in the operation manual;
c. The operator, or a designated responsible
maintenance person for a privately operated sewage pumping station, is
knowledgeable in operation of the portable generator or pumping equipment and
will be on call 24 hours per day, 7 days per week;
d. The pump station wet well provides additional
storage volume above the high-water level alarm and below all entering and
existing pipes to allow for deployment of the portable generator or pumping
equipment; and
e. The additional wet well storage volume provides at
least 6 hours detention at average daily flow; and
(2) For sewage
pumping stations with duplex pumps, a standby engine drive system which
automatically starts on power loss to drive one pump may be furnished as an
alternative to a permanent generator.
(k) Sewage pumping station by-passes shall not
discharge raw sewage either overland or to any water course.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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PART Env-Wq 706
SITING OF WWTPs
Env-Wq 706.01 WWTP
Location.
(a) WWTPs shall be located and designed such that
the impact of possible odor problems and safety and health problems to the
adjacent properties are minimized to the extent practicable.
(b) Factors to consider when siting a WWTP shall
include, but not be limited to, the following:
(1) The type of
WWTP to be constructed and the level of odors that typically are generated by
that type of WWTP;
(2) The current
and projected land use surrounding the proposed site;
(3) The current
and projected population surrounding the proposed site;
(4) The
direction of prevailing winds in relation to populated areas;
(5) The
proposed location’s susceptibility to flooding;
(6)
Regionalization options of WWTPs for sewage and septage receiving;
(7) Impacts to
surface waters, wetlands, habitat, and wildlife, including any threatened or
endangered species;
(8) Traffic
impacts on surrounding areas;
(9) Potential
for effluent reuse; and
(10) Such
additional information as is collected for the environmental review required by
Env-Wq 500, if applicable.
Source. (See Revision Note at chapter heading for
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Env-Wq 706.02 Buffer
Distances. Buffer distances shall be
as follows:
(a) Wastewater treatment ponds shall be located
not closer than 600 feet from any residence; and
(b) Processing units in a conventional WWTP shall
be located not closer than 300 feet from any residence.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 706.03 Flooding.
(a) Existing WWTPs and pump stations shall be:
(1) Designed to
provide for uninterrupted operation of all process units during a 25-year
flood; and
(2) Be placed
above or otherwise protected against damage from a 100-year flood.
(b) New and modified critical components of WWTPs and pump
stations shall be:
(1)
Designed
to provide for uninterrupted operation of all process units during a 100-year
flood; and
(2)
Be placed
above or otherwise protected against damage from either:
a. A water
surface that is 3 feet above the 100-year flood elevation;
b. The 500-year
flood elevation; or
c. An elevation
determined from a best available scientific approach defined in (e)(3),
below.
(c)
Critical WWTP components which shall be protected from flooding
include:
(1) Preliminary treatment;
(2) Influent pumping;
(3) Primary treatment and sludge pumping;
(4) Secondary treatment and sludge pumping;
(5) Intermediate pumping;
(6) Advanced treatment;
(7) Disinfection;
(8) Effluent pumping;
(9) Power and electrical systems;
(10) Control, communication, and alarm systems; and
(11) Emergency generators.
(d)
Critical pump station components which
shall be protected from flooding include:
(1) Pumping equipment;
(2) Power and electrical systems;
(3) Control, communication, and alarm systems; and
(4)
Emergency generators.
(e) Subject to
(f) below, flood elevations shall be determined using:
(1) Flood maps;
(2) Methods
defined in Env-Wq 1503.09 (f)(1) and (f)(2); or
(3) A best available scientific approach that uses readily
available, actionable hydrologic and hydraulic data, and methods that integrate
current and future changes in flooding based on latest climactic predictions.
(f) If the project is for infrastructure having a projected
life that extends beyond 2050 and is within at least one of New Hampshire’s 17
coastal zone municipalities, including Dover, Durham, Exeter, Greenland,
Hampton, Hampton Falls, Madbury, New Castle, Newfields, Newington, Newmarket,
North Hampton, Portsmouth, Rollinsford, Rye, Seabrook, and Stratham,
determination of the flood hazard elevation specified in (b) and (e) above
shall address projected storm surge, sea level rise, and precipitation events
identified in the “New Hampshire Coastal Flood Risk Summary – Part I: Science
and Part II: Guidance for Using Scientific Projections" prepared for the
New Hampshire Coastal Flood Risk Science and Technical Advisory Panel 2019,
available as noted in Appendix B. A representative concentration pathway (RCP) of
RCP 4.5 or higher and a “low” or “very low” tolerance for flood risk shall be
applied.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 706.04 Effluent Quality. The degree of treatment
provided at a WWTP shall be designed to meet the effluent discharge limitations
and water quality standards established by applicable provisions of:
(a) The state
surface or ground water discharge permit;
(b) Env-Wq 1700,
relative to surface water quality standards;
(c) The federal
surface water discharge permit; or
(d) The Clean
Water Act.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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PART Env-Wq 707
BASIS OF DESIGN REPORTS FOR WWTPs
Env-Wq 707.01 Basis
of WWTP Design.
(a) The WWTP design shall provide flexibility for
operating within the expected range of wastewater characteristics and volumes.
(b) A pilot test that complies with Env-Wq 717.04
shall be conducted for a proposed treatment technology if:
(1) Effluent
permit limits are at or near the limits of the proposed treatment technology;
(2) Anticipated
wastewater characteristics:
a. Are not
typical of those commonly received by a WWTP due to low- or high-strength
effluent, high strength sidestreams, or industrial
waste contributions; and
b. Have a
recognized potential to adversely affect the performance of the proposed
treatment process; or
(3) Extreme
weather or population fluctuations have a recognized potential to adversely
affect the technology’s performance.
(c) The owner shall submit a basis of design
report as described in Env-Wq 707.02 through Env-707.07 to the department for
review and approval prior to final design.
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Env-Wq 707.02 Basis of Design Report: Project Planning. Relative to
general WWTP information and project planning, the basis of design report shall
include a description or analysis of:
(a) Character and use of the receiving waters;
(b) Location and topography of the WWTP site,
including:
(1) Scale maps
and topographical maps depicting natural boundaries in the project area and any
existing service areas; and
(2) Photographs
of the project area and any existing service areas;
(c) Population trends and anticipated future
growth, by including with the basis of design report population projections
based on historical population data from the United States Census Bureau for no
less than 20 years prior to submission of the basis of design report, if
available;
(d) Environmental resources present using maps,
photographs,
and narrative description as available; and
(e) A public participation and education plan,
including:
(1) Education
relative to need for the project;
(2) Utility
operational service levels required; and
(3) Funding and
revenue strategies to be used.
Source. (See Revision Note at chapter heading for
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Env-Wq 707.03 Basis of Design Report: Existing Facilities. For existing
facilities, the basis of design report shall include a description or analysis
of:
(a) Existing facilities, including:
(1) Condition
of existing facilities, including:
a. Adequacy of
current facilities;
b. Suitability
for continued use;
c. Conveyance,
treatment, storage, and disposal capabilities;
d. Existing
capacity of each component;
e. Analysis of
overall current energy consumption; and
f. Reference an
asset management program, if applicable;
(2) Location
maps of existing facilities;
(3) Schematic
process layout of all existing facilities;
(4) Summary of
recurring compliance issues; and
(5) History of
major system components, including:
a. Operational
history;
b. Renovations;
and
c. Expansions;
(b) Current financial status of existing
facilities, including:
(1) Current
rate schedules;
(2) Annual
operation and maintenance costs with a breakout of current energy costs;
(3) Other
capital improvement programs;
(4) Tabulation
of users by monthly usage categories for the most recent fiscal year; and
(5) Status of
existing debts and required reserve accounts;
(c) Water, energy, or waste audits and outcomes
thereof, if applicable;
(d) Existing and projected flow;
(e) Flow composition, waste strength, and
peaking factors based on historical records, if records exist;
(f) If no records exist, domestic waste strength
and peaking factors based on:
(1) An average
daily per capita contribution of 0.20 pounds of TSS and 0.17 pounds of BOD5,
if garbage grinders are not prevalent in
the area;
(2) An average
daily per capita contribution of 0.25 pounds of TSS and 0.22 pounds of BOD5,
if garbage grinders are prevalent in the area;
(3) An average
daily per capita contribution of 0.04 pounds of total nitrogen;
(4) An average
daily per capita contribution of 0.006 pounds of total phosphorous; and
(5) Not less
than 70 gallons of flow per capita per day nor more than 100 gallons of flow
per capita per day;
(g) For process-related upgrades to existing WWTPs, or where sampling of
the future influent wastewater stream is possible, the sampling results for the
following influent wastewater parameters from plant records for the previous 2
years or, if such data is not available, from sampling designed by the engineer
to produce representative results:
(1) Biochemical Oxygen Demand (BOD5);
(2) Total Suspended Solids (TSS);
(3) pH;
(4) Temperature;
(5)
Total
Kjeldahl Nitrogen (TKN);
(6) Alkalinity;
(7) Chemical Oxygen Demand (COD), as applicable; and
(8) Total Phosphorous, as applicable;
(h) Industrial wastes, if present, quantified, and
characterized as follows:
(1) Use an
industry-by-industry chemical analysis from existing pretreatment programs
including conventional pollutants (BOD5 and TSS), nutrients, pH, and
non-conventional parameters potentially present in the waste stream; or
(2) In the
absence of existing pretreatment programs, full waste characterization shall be
performed; and
(i) Septage receiving
and treatment capacity, based on:
(1) The septage
volume and characterization expected to be received during the planning period
of the WWTP;
(2) Septage
strength of 6,500 mg/L BOD5, 12,900 mg/L TSS, 590 mg/L total
Kjeldahl nitrogen (TKN), and 210 mg/L total phosphorous, if specific data is
not available; and
(3) Appropriate
peaking factors to account for seasonal variations in septage quantities from
the specific service area.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 707.04 Basis of Design Report: Project Need. For existing
and proposed projects, the basis of design report shall address the need for
the project based on a description or analysis of the following:
(a) Conditions requiring improvements;
(b) The design period for the WWTP, which shall
be not less than 20 years unless
a shorter design period is shown to be more cost effective when taking into
consideration construction of additional facilities needed to meet the peak
demand of the 20-year design period;
(c) A design period evaluation, which shall include:
(1) An
evaluation of future expansion requirements in excess of the planning period,
when laying out and designing major treatment units and WWTP hydraulics;
(2) Design
flows for domestic, commercial, industrial, and infiltration/inflow (I/I) flows,
as applicable;
(3) Stormwater
flows, for WWTPs with combined sewers within the service area;
(4) Design flow
values, including the following:
a. Annual
average flows;
b. Peak hourly
flow;
c. Maximum
daily flow;
d. Maximum
monthly flow;
e. Minimum
monthly flow; and
f. Minimum
daily flow;
(5) Total
influent TSS and BOD5 loading, calculated as the sum of domestic,
commercial, industrial, and septage loads throughout the design period of the
WWTP; and
(6) A mass
balance, performed as follows:
a. The mass
balance shall be prepared for average conditions and appropriate peaking
factors used for peak design conditions;
b. The mass
balance shall include BOD5 and TSS loadings for each appropriate process and
for all side streams;
c. The mass
balance shall include nutrient loadings when the WWTP is designed for nutrient
removal; and
d. Sidestream flows returned to the liquid treatment process
as the result of sludge, scum, or other floatable matter processing shall be
characterized as to solids and organic content, with the characterization being
included in the design loadings for both liquid and solids treatment processes;
(d) Relative to WWTP hydraulics, the basis of
design report shall address the following:
(1) Hydraulic
profiles of each treatment process on the design drawings indicating water
surface elevations for peak hourly and annual average design flows against the following receiving water levels:
a. The average
level;
b. The 100 year
level; and
c. The flood
level defined in Env-Wq 706.03(b)(2);
(2) Hydraulic
design under peak hourly flow conditions, including associated sidestream flows, to be passed through the WWTP with the
largest or longest flow path of each unit process removed from service;
(3) Design
allowance for maximum flows to pass through the WWTP when and if the largest
pump or other piece of mechanical equipment is out of service; and
(4) A minimum
velocity of 2.0 feet per second at design annual average flow and 1.5 feet per
second at minimum flow in channels carrying unsettled wastewater unless
wastewater is managed to prevent sedimentation of solids;
(e) Present and proposed future discharge permit
limits, if any; and
(f) The effect on the wastewater treatment
process of industrial wastes likely to be encountered in the influent waste
stream.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 707.05 Basis
of Design Report: Treatment Technology Options Considered. For each
treatment technology option considered, the basis of design report shall
include a description or analysis of:
(a) The facilities associated with each proposed
treatment technology option;
(b) Design calculations and parameters used for
sizing the unit processes and components for evaluation purposes to demonstrate
compliance with all applicable federal and state design requirements;
(c) Environmental impacts, including:
(1) Direct and
indirect impacts on floodplains, wetlands, land resources, endangered species,
and properties of historical and archeological significance;
(2) Generation
and management of residuals and wastes; and
(3)
Sprawl-related impacts;
(d) Sustainable utility management practice
considerations, including:
(1) Water and
energy efficiency, including:
a. Water reuse
and conservation;
b. Energy
efficient design to reduce electrical demand and minimize carbon footprint,
including:
1. Blower and
pump sizing to provide energy-efficient operation at a full range of flow
rates;
2. Use of
premium efficiency motors;
3. Installation
of heat recovery systems; and
4. Use of
biogas capture and reuse if digesters are proposed;
c. Renewable
energy generation, if applicable to the treatment technology option; and
d. Water and
energy usage of each option as compared to other treatment technology options;
(2) Aspects of
project that preserve or mimic natural processes to manage onsite stormwater,
if applicable to the treatment technology option; and
(3) Site
management of stormwater runoff volume and peak flows through infiltration,
evapotranspiration, harvest, and use, if applicable;
(e) Ultimate sludge disposal plans, including
contingency plan as required by Env-Wq 716 for sludge stabilization, sludge
thickening, and sludge dewatering; and
(f) Estimates of capital and operating costs for
each treatment technology option, including:
(1)
Construction costs;
(2) Total
project costs;
(3) Average
annual operation and maintenance costs over the life of the project; and
(4) Energy
costs.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 707.06 Basis of Design Report: Life Cycle Comparison of Treatment Technology
Options. For life cycle comparison of treatment
technology options, the basis of design report shall include a
description or analysis of:
(a) Capital, operation, and maintenance costs, including
energy costs;
(b) Life cycle comparison over a 20-year planning
period unless an alternative length planning period is justified;
(c) Discount rates, based on the discount rate
set forth in Appendix C of OMB circular A-94 available at https://www.whitehouse.gov/wp-content/uploads/2023/12/CircularA-94AppendixC.pdf;
(d) Present worth analysis using total project
cost including construction and non-construction costs;
(e) Average annual operation and maintenance
costs over the life of the project, converted to present day dollars using a
uniform series present worth calculation;
(f) Deductions of the present worth of the
salvage value;
(g) Net present value calculations for each
evaluated treatment technology option; and
(h) Non-economic factors such as social and
environmental aspects, including, but not limited to:
(1)
Reliability;
(2) Operational
complexity;
(3)
Expandability; and
(4)
Sustainability.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 707.07 Basis of Design Report: Proposed Project – Recommended
Treatment Technology. The basis of design report shall include a
recommended treatment technology and a description or analysis of:
(a) The selected treatment technology, explaining
justification for making the selection over other available treatment
technology options;
(b) Design criteria summary;
(c) Site layout and hydraulics profile;
(d) Treatment process schematics;
(e) Cost summary;
(f) For a proposed modification or addition to an
existing WWTP, a construction sequence for maintaining WWTP operations and
permit compliance during construction and testing; and
(g) An overall project schedule from design
through completion of construction that also includes the meetings between the
owner, design engineer, and department review staff required by Env-Wq 707.08
and any additional meetings considered necessary by the owner and design
engineer.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 707.08 Meetings
Required.
(a) The owner and design engineer shall meet with
department review staff:
(1) At or prior
to project initiation for the purpose of outlining project scope and goals; and
(2) Upon
completion of the basis of design report for the purpose of reviewing report
recommendations, department comments on the report, and project progression
plans.
(b) If one or more meetings with the department
in addition to those included in the project schedule are considered necessary
for the project progression by the owner and design engineer, the design
engineer shall contact department review staff to schedule such meeting(s).
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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PART Env-Wq 708
ADDITIONAL WWTP REQUIREMENTS
Env-Wq 708.01
Installation and Initial Operation. For items of equipment that are essential to
the treatment process, the owner shall have a
representative of the manufacturer:
(a) Inspect
the installation; and
(b) Supervise the initial operation.
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Env-Wq 708.02 Required
Redundancy.
(a) Standby units shall be provided for all
critical components as defined in Env-Wq 706.03.
(b) For pumps and other critical hydraulic
components, the WWTP shall have one standby unit for every 3 units, or fraction
thereof, required to handle peak design flow or load.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq 708.03 Planning for Unit Process Maintenance and Dewatering
Required.
(a) The WWTP shall be designed to facilitate unit
process maintenance such that:
(1) Each unit
of the WWTP can be removed from service independently;
(2) The design
facilitates WWTP operation during unit maintenance and emergency repair so as
to minimize deterioration of effluent quality;
(3) Solids
retention, sludge handling, and disinfection are addressed as specified in this
chapter; and
(4) WWTP
by-passes that allow raw or insufficiently treated sewage to be discharged
directly to a water course are prevented.
(b) For WWTP upgrade or expansion, the technical
specifications prepared per Env-Wq 703.02 shall include a detailed description
of how to maintain existing WWTP operations, delineating the suggested
construction sequence and number of units to be removed from treatment
operation.
(c) A means of unit isolation and dewatering
shall be provided for each process unit.
(d) Each tank shall be protected against
flotation.
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Env-Wq 708.04 Piping
and Flow Distribution Devices.
(a) Piping and channels throughout the WWTP shall
be designed to carry the maximum design flows as follows:
(1) Gravity
influent sewers shall not be surcharged during normal operating conditions;
(2) Bottom
channel corners shall be filleted, with the elimination of pockets and corners
where solids can accumulate;
(3) Suitable
gates, stop logs, or plates shall be placed in channels to seal off unused
sections that might accumulate solids;
(4)
Non-corrodible materials shall be used for gates; and
(5) Channels
that might
not be used for considerable periods of time shall have valved drains.
(b) Flow distribution devices shall be designed
to:
(1) Control
organic, solids, and hydraulic loading to WWTP process units;
(2) Provide
distribution to individual treatment units to ensure equal distribution among
all units;
(3) Provide
visible status indication for influent flow to each unit via weirs, sluice
gates, slide gates, control valves, or other means;
(4) Provide
positive scum and foam removal in all channels and distribution structures that
have a trapped-free surface; and
(5) Not rely on
effluent weirs and flow route symmetry for flow control.
(c) Underflow shear gates for balancing flows
shall not be permitted.
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Env-Wq 708.05 WWTP Design and Layout. In addition
to complying with applicable federal, state, and local building requirements,
the design and layout of WWTPs, including building interiors and mechanical
layouts, shall include provisions for future expansion and upgrades as follows:
(a) Locations of foreseeable future facilities
shall be indicated on the construction drawings;
(b) WWTP hydraulics, sizing of conduits
connecting unit processes, and flow distribution shall provide for future
expansion; and
(c) Plugs, blind flanges, sluice gates, and
valving shall be designed to facilitate expansion with minimal disruption to
operating facilities.
Source. (See Revision Note at chapter heading for
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Env-Wq 708.06 Design and Layout of Chemical Feed Equipment: Storage
Requirements. General equipment design shall meet the
following criteria so as to allow for the continuous supply of accurate amounts
and rates of chemicals throughout the range of feed requirements:
(a) Materials and surfaces that will come in
contact with chemicals or solutions thereof shall be resistant to the chemicals
and their solutions, with corrosive chemicals being introduced in a way that
minimizes the potential for corrosion;
(b) Chemicals that are incompatible shall not be
stored or handled together;
(c) Liquid chemical storage tanks in excess of 55
gallons shall have a liquid level indicator and:
(1) An overflow
and a contained receiving basin; or
(2) A drain
capable of receiving and containing accidental spills or overflows equal in
volume to 110 percent of the storage tank capacity;
(d) All liquid chemical storage tanks shall be
properly labeled;
(e) The day tank or solution tank, if provided,
shall provide a means to maintain a uniform solution strength;
(f) Overflow pipes shall:
(1) Have a
submerged discharge to a containment vessel;
(2) Be visible
to the operator under normal operating conditions; and
(3) Be marked
to designate the pipe’s origin tank and the chemical being conveyed;
(g) Acid storage tanks shall be vented to the
outside atmosphere, with each tank having a separate vent and a valved drain to
protect against backflow;
(h) Carts, elevators, hoists, and other
appropriate means for lifting chemical containers shall be provided;
(i) Provision shall
be made for the proper transfer of dry chemicals from shipping containers to
storage bins or hoppers, in a way that minimizes dust entering the room where
the equipment is installed;
(j) Ventilation or personal protection, or both,
shall be provided to prevent operator exposure to dust and chemicals, whether
in the storage, transfer, or application areas;
(k) Vents from feeders, storage facilities, and
equipment exhaust shall discharge to the outside atmosphere above grade and
away from air intakes; and
(l) Interior floor drains in chemical storage
areas shall discharge to a holding tank.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.07 Design and Layout of Chemical Feed Equipment: Feed
Requirements.
(a) A separate feeder shall be used for each
chemical applied.
(b) Chemical feeders shall be manually and
automatically controlled with the automatic controls designed to allow override
by the manual controls.
(c) Chemical feed rates shall be adjustable based
on appropriate control parameters.
(d) Dry chemical feeders shall measure chemicals
volumetrically or gravimetrically and provide adequate solution water and
agitation of the chemical in the solution tank.
(e) Water supply for chemical feed applications,
when needed, shall be sufficient in quantity and pressure for the intended
application.
(f) A means of measuring supply water shall be
provided when preparing specific solution concentrations by dilution.
(g) The water supply shall be treated as
necessary to ensure compatibility with its intended use.
(h) Chemical feed equipment shall be located in a
dedicated room or area to reduce hazards and dust problems.
(i) The length of
feed lines shall be minimized by locating the equipment as close to the
application point(s) as practical.
(j) The chemical feed equipment shall be
accessible for servicing, repair, and observation of operation.
(k) Feed lines shall be:
(1) As short as
possible;
(2) Easily
accessible along the line’s entire length;
(3) Protected
from freezing;
(4) Readily
cleanable; and
(5) Color coded
and labeled.
(l) Color coding of WWTP piping and chemical feed
lines shall:
(1) For
upgrades to existing plants, comply with either the existing WWTP color coding
system or section 4.4.5 of TR-16, “Guides for the Design of Wastewater
Treatment Works” by the New England Interstate Water Pollution Control
Commission, revised 2016 edition, available as noted in Appendix B; and
(2) For all new
WWTPs, comply with color codes specified in section 4.4.5 of TR-16, ”Guides for
the Design of Wastewater Treatment Works” by the New England Interstate Water
Pollution Control Commission, revised 2016 edition, available as noted in
Appendix B.
(m) When conveying gases, the feed lines shall
slope upward from the chemical source to the feeder.
(n) Provision shall be made for measuring
quantities of chemicals used to prepare feed solutions.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.08 Operation
and Maintenance Manuals.
(a) Operation and maintenance manuals providing
information and guidance for day-to-day operation of the WWTP shall be
submitted to the department for review and approval within 60 days following
substantial completion of construction of the WWTP.
(b) The operation and maintenance manuals
required by (a), above, shall include all information that is necessary to
operate and maintain the specific equipment at the WWTP, including but not
limited to the following:
(1) Information
on process design assumptions;
(2) Unit
process information that includes detailed process descriptions and accepted
parameters, control measures, and monitoring procedures for the various processes;
(3) Start-up
procedures for each unit operation and piece of equipment;
(4) Maintenance
management systems;
(5) Laboratory
test procedures;
(6) Safety
procedures;
(7)
Organizational structure and administrative procedures;
(8)
Troubleshooting procedures;
(9) Emergency
operation plan;
(10) Staffing
requirements;
(11) Process
and instrumentation diagrams;
(12) Checklists
for systems and components for the operator’s use in developing a maintenance
program for WWTPs;
(13) Utility
emergency contact information;
(14) Staff
training and licenses necessary for chief operator and assistant operator;
(15) A list of
each chemical used in process and what the chemical is used for, together with
the applicable MSDS ; and
(16) Equipment
supplier manuals.
(c)
The department shall approve an
operation and maintenance manual if it contains all the requirements in (b),
above.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.09 Site
Access.
(a) WWTP access roads shall provide access to all
delivery and loading points.
(b) Roadway design and construction details
shall be as required for the types of vehicles that will access the site and in
accordance with local and state requirements.
(c) Access to the site shall be controlled with a
perimeter fence and lockable gate(s).
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.10 Site
Grading.
(a) Grading or drainage systems for the WWTP
site shall be designed to handle surface runoff.
(b) All-weather walkways shall be provided for
access to all units.
(c) Surface water shall not be permitted to
drain into any process unit.
(d) Drains and runoff in areas contaminated by
sludge or wastewater shall discharge to the treatment facilities for
processing.
(e) Drainage from chemical storage and handling
areas shall discharge to the WWTP for processing.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.11 Outside Lighting. Outside units, tanks,
equipment, and work areas shall be lit using energy efficient lighting so as to
allow safe inspection of the facility in all ambient conditions.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.12 Floor Slope. Floor surfaces shall be sloped to allow
drainage to a point of collection such as a sump or drain.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.13 Access
to Equipment.
(a) Suitable openings, hatches, or other means
shall be provided for removal of machinery and equipment.
(b) Openings shall be large enough to allow for
removal of the largest piece of equipment or largest component if equipment is
disassembled.
(c) Lifting devices, properly sized for the
required loads, shall be provided for removal of equipment.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.14
Essential Power Requirements for WWTPs.
(a) Subject to (b), below, power shall be
provided at all times to operate essential equipment including, but not limited
to:
(1) Preliminary
treatment;
(2) Influent
pumping;
(3) Primary
treatment;
(4) Critical
secondary treatment;
(5)
Intermediate pumping;
(6) Other
critical treatment processes;
(7)
Disinfection;
(8) Effluent
pumping;
(9) Lighting
and ventilation that is essential to the safe operation of the WWTP; and
(10) Alarm
systems and essential controls.
(b) An owner shall not be required to provide
power to operate all essential components at all times if the owner develops
and obtains department approval for an alternate load management plan pursuant
to (c) and (d), below.
(c) The alternate load management plan shall
contain the following:
(1) A
demonstration that the discharge limits set forth in the WWTP’s discharge
permit will continue to be met during the emergency generator operation;
(2) A
description of the electrical load imposed by various pieces of equipment,
ranked by importance and ability to by cycled;
(3) A
description of the maximum and minimum amount of time process equipment can be
operated without adversely effecting wastewater operations; and
(4) A list of
equipment that the WWTP cannot run without operating and demonstrate the
available emergency power available for that minimum load.
(d) The department shall approve the alternate
load management plan if it determines that the plan will allow the WWTP to
operate as needed to not violate its discharge permit.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.15 Instrumentation and Control Requirements. Any
supervisory control and data acquisition (SCADA) system included in the design
shall have the following minimum capabilities:
(a) Air flow rate and flow pacing of blowers;
(b) Alarm generation and history;
(c) Influent flow history and trending;
(d) Dissolved oxygen history and trending;
(e) Power monitoring for main process pumps and
motors and blowers and motors, including at a minimum the ability to monitor:
(1) Power
factor data at equipment startup;
(2) Total
harmonic distortion; and
(3) Total
energy usage;
(f) Return activated sludge pump flow rate and
pacing;
(g) Real time monitoring and recording of energy
use; and
(h) Automated equipment system monitoring and
control for the following, as applicable:
(1) Pumps;
(2) Chemical
feed systems;
(3)
Disinfection;
(4) Aeration
system;
(5) Digester;
and
(6) Dewatering.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.16 Essential Water Supply Requirements for WWTPs.
(a) A pressurized potable water supply shall be
provided for firefighting and use in the WWTP.
(b) No piping or other connections shall exist in
any part of the WWTP or collection system that might cause the contamination of
a potable water supply.
(c) The chemical quality of the water supply shall
be checked for suitability for its intended uses such as heat exchangers and
chlorinators.
(d) Potable water from a municipal or separate
supply may be used directly at points above grade for the following hot and
cold supplies with no additional backflow protection:
(1) Lavatory
sinks;
(2) Toilets;
(3) Showers;
(4) Drinking
fountains;
(5) Laboratory
sinks, if protected against back siphoning; and
(6) Slop sinks,
if protected against back siphoning.
(e) All potable water supply mains shall be
protected against contamination with a reduced-pressure-zone backflow preventer
that meets the requirements of Env-Dw 505, including local approval if
required.
(f) Hot water for any unit cited in (d), above,
shall not be taken directly from a boiler used for supplying hot water to a
sludge heat exchanger, digester heating coils, or similar process.
(g) Where a public water supply is not available,
a separate drilled well shall be provided as a potable water supply.
(h) Where a potable water supply will be used
for any purpose other than those listed in (d), above, a backflow protection
device that meets the requirements of Env-Dw 505, including local approval if
required, shall be installed.
(i) Vacuum
breakers shall be installed on the water supply to the laboratory.
(j) The number of backflow devices required shall be
minimized by providing a separate, non-potable, in-plant water system using a
single backflow protection device.
(k) A sign shall be permanently posted at each
hose bib, sill cock, or other fixture on the non-potable water system
indicating that the water is not safe for drinking.
(l) Where break tanks are used for backflow
prevention, water shall discharge to the break tank through an air-gap at least
6 inches above the maximum flood line or the spill line of the tank, whichever
is higher.
(m) Where a separate non-potable water supply
will be provided, a backflow prevention device shall not be required.
(n) Hydrants for fire protection and hydrants
for yard use shall:
(1) Be clearly
distinguished from one another with different paint colors; and
(2) Have
different-sized nozzles for hose connections.
(o) Locations of fire protection hydrants shall
be approved by the appropriate local official.
(p) Hydrants fed by the potable water supply
system shall be protected from cross-contamination as required by the owner of
the water system.
(q) Toilets and showers shall be provided for
the projected number of operators with separate toilets and showers for men and
women.
(r) Slop sinks for general cleaning shall be
provided.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.17 Wastewater
Flow Measurement.
(a) Means for measuring, recording, and totaling
both raw influent flow prior to sidestreams and
effluent wastewater flow after WWTP water withdrawal shall be provided.
(b) Provisions for measuring, recording, and
totaling the flow of return activated sludge, primary sludge, waste secondary
sludge, and other major sludge streams shall be provided.
(c) All flow measurement equipment shall be:
(1) Sized to
perform effectively over the full range of expected flows; and
(2) Protected
against freezing.
(d) Installation of flow measuring equipment
shall be such that the required hydraulic conditions necessary for accurate
measurement are provided.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.18 Sampling.
(a) Sampling sites shall:
(1) Be readily
accessible by WWTP personnel;
(2) Not be
located in confined space areas;
(3) Be free of
tripping, slipping, and falling hazards;
(4) Have a
supply of electrical power with a ground fault interrupt; and
(5) Be supplied
with batteries or connected to the emergency power source.
(b) To prevent freezing, samplers shall be housed
in enclosed and, if needed, heated structures or equipment enclosures designed
for outdoor use.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.19 WWTP
Outfalls.
(a) Provision shall be made for effective
dispersion of the effluent into the receiving water body so as to meet the
water quality criteria as specified in Env-Wq 1700.
(b) The outfall pipe outlet(s) shall be
submerged at all times.
(c) The outfall pipe shall be so constructed and
protected against the effects of flood water, tides, ice, or other hazards as
to reasonably ensure its structural stability and freedom from stoppage.
(d) Outfall pipes shall not impede or otherwise
interfere with navigation.
(e) A manhole shall be provided at the shore end
of all gravity outfall sewers extending into the receiving stream.
(f) Outfall pipe and fittings shall be
constructed of ductile iron, HDPE, or PVC material.
(g) All ductile iron pipe shall be corrosion
protected if installed in a corrosive environment that could reduce the typical
life expectancy of the pipe.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.20 Safety. The
following features shall be incorporated into the design and construction of
WWTPs for the protection of visitors and facility operations staff:
(a) Hand rails, guards, safety netting, and
barricades around tanks, trenches, pits, stairwells, floor openings,
maintenance access areas, and other hazardous structures;
(b) Gratings over areas of treatment units where
access for maintenance is required;
(c) First aid equipment;
(d) Appropriately placed warning signs and
labels as per the NFPA as incorporated by reference in the state fire code in
Saf-C 6000 and NFPA 820, available as noted in Appendix B, and New Hampshire department
of labor requirements as specified in Lab 1400 in, but not limited to, the
following areas:
(1) Slippery
areas;
(2) Non-potable
water fixtures;
(3) Low head
clearance areas;
(4) Open
service manholes;
(5) Hazardous
chemical storage areas
(6) Flammable
fuel storage areas; and
(7) Confined
spaces;
(e) Personal protective clothing and equipment
as per New Hampshire department of labor requirements as specified in Lab 1400,
to include:
(1) Eye, ear,
and face protection;
(2) Respiratory
protection; and
(3) Head, hand,
and foot protection;
(f) Gas detectors for use in occupied areas rated
under the NEC, as adopted by reference in the state building code pursuant to
RSA 155-A:1, IV, as Class 1, Division 1,
Group A, B, C, and D locations or areas classified as Class 1 Division 2
through the use of mechanical ventilation per the NFPA as incorporated by
reference in the state fire code in Saf-C 6000 and NFPA 820, available as
noted in Appendix B;
(g) Provisions and equipment for permit-required
confined space entry in accordance with New Hampshire department of labor
requirements as specified in Lab 1400;
(h) Ventilation of enclosures in accordance with
the NFPA as incorporated by reference in the state fire code in Saf-C 6000 and
NFPA 820,
available as noted in Appendix B;
(i) Fire protection
systems and equipment; and
(j) Machinery guards around belts or other moving
parts.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.21 Hazardous
Chemical Handling.
(a) The materials used for storage, piping,
valves, pumping, metering, and splash guards shall be specially selected so as
to be compatible with the physical and chemical characteristics of each
hazardous or corrosive chemical that will be used at the WWTP.
(b) Chemical storage areas shall be enclosed in
dikes or curbs that will contain the stored volume until the spilled chemical
can be safely transferred to alternative storage or released to the wastewater
at controlled rates that will not damage facilities, inhibit the treatment
processes, or contribute to stream pollution.
(c) Eye wash fountains and deluge showers using
potable water shall be:
(1) Provided in
the laboratory and on each floor or work location involving hazardous or
corrosive chemical storage, mixing or slaking, pumping, metering, or
transportation loading;
(2) As close as
practicable to possible chemical exposure sites; and
(3) Fully
usable during all weather conditions.
(d) Eye wash fountains, including self-contained
eye wash fountains and eye wash stations, and deluge showers shall be designed
in compliance with the ANSI/ISEA Z358.1-2014 standard, available as noted in Appendix B. If
the water heater system for the eye wash fountains and deluge showers is not
separate from the WWTP hot water supply, mixing valves with scald protection
shall be provided to maintain the required water temperature.
(e) All piping containing or transporting
corrosive or hazardous chemicals shall be identified with labels every 10 feet
and with at least 2 labels in each room, closet, or pipe chase. Pipes containing hazardous or corrosive
chemicals shall not be located above shoulder level except where continuous
drip collection trays and coupling guards will eliminate chemical spray or
dripping onto personnel.
(f) All pumps, feeders, connections, and
couplings for hazardous or corrosive chemicals shall have guards that will
effectively prevent spray of chemicals into space occupied by personnel. The splash guards shall be in addition to
guards intended to prevent injury from moving or rotating machinery parts.
(g) All hazardous waste generated shall be
managed in accordance with RSA 147-A and Env-Hw 100-1100.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.22 Laboratory
Equipment.
(a) Subject to (b), below, all WWTPs shall
include a laboratory and the equipment needed for wastewater analysis, process
control tests, discharge permit tests, and quality control analysis checks.
(b) If the owner chooses to not include a
laboratory in the WWTP, the owner shall contract with an outside laboratory for
all testing services specified in (a), above.
(c) Laboratories shall be ventilated in
accordance with the NFPA as incorporated by reference in the state fire code in
Saf-C 6000 and NFPA 820, available as noted in Appendix B.
(d) Laboratory floor surfaces shall be
slip-resistant and fire-resistant, as well as highly resistant to acids,
alkalis, solvents, and salts.
(e) The laboratory shall have at least 2 exit
doors, with glass windows for easy visibility, to allow for straight
egress. Panic hardware shall be
installed on all doors.
(f) Vacuum break type faucets shall be supplied
for laboratory sinks. Plumbing shall be
based on the types of substances that might be discarded in the drain lines, with
acid- or chemical- resistant waste drain lines being installed as needed.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.23 WWTP
Alarms.
(a) Alarm systems shall be included to notify
WWTP operators of any circumstance or condition that threatens public health or
safety or the ability of the WWTP to provide adequate treatment of the
wastewater in accordance with the effluent limitations set forth in the
discharge permit.
(b) A 24 hour per day, 7 day per week
notification system shall be installed at the WWTP control room. Where a WWTP is not manned on a 24 hour per
day basis, an additional notification system shall be installed at the police
station, fire station, or any other locale having 24 hour per day manning,
including a commercial dispatch service or SCADA enunciation system.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 708.24 Testing. All
liquid containing vessels and structures shall be leak tested prior to
operation in accordance with manufacturer’s recommendations and any applicable
industry standards and regulatory requirements.
Any visible signs of leakage shall be repaired and retested prior to
placing the unit in service.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
708.25 Septage Receiving Stations. Any septage receiving station shall have:
(a) Drainage tied into the WWTP process to
prevent run off of spilled septage; and
(b) For gravity off-loading systems, grading such
that septage trucks can be completely off-loaded by gravity.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 709
INFLUENT HEADWORKS
Env-Wq
709.01 Screening Devices: Location,
Operation, and Maintenance.
(a) Each WWTP shall have mechanized screening for
influent sewage that operates continuously or using automated controls.
(b) Any screening device installed in a building
where other equipment or offices are located shall be separated from the rest
of the building and provided with separate outside entrances and mechanical
ventilation.
(c) Each mechanical screening unit shall have
controls that:
(1) Cause the
cleaning mechanism to operate at a predetermined high water level; and
(2) Allow the
mechanism to operate on a timing device.
(d) Facilities for removal, handling, storage,
and disposal of screenings in a sanitary manner shall:
(1) Include an
accessible platform from which the operator can rake screenings easily and
safely if cleaned manually; and
(2) Have drains
for the platform area and all storage areas.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 709.02 Screening
Devices: Design and Capacity.
(a) Each by-pass screen device shall have clear
openings between bars from 1.0 to 1.75 inches wide.
(b) Clearance between bars on coarse racks or
screens preceding mechanically-cleaned screens may be greater than 1.75 inches.
(c) Manually-cleaned screens shall be:
(1) Designed
and installed to accommodate being cleaned;
(2) Be placed
on a screen slope of 30 to 45 degrees with the horizontal if for non-emergency
use; and
(3) Used only
in by-pass channels.
(d) Clear openings for mechanical screens other
than by-pass screens and preliminary screens or racks shall be ½-inch or less
to maximize removal of inert material.
(e) For manually-cleaned bar screens, the screen
chamber shall be designed to provide a velocity through the screen of one foot
per second at an average rate of flow calculated from design average daily
flow.
(f) For mechanically cleaned screens, maximum
velocities during wet weather periods shall not exceed 2.5 feet per
second, calculated based on the vertical open cross-sectional area below
the flow line.
(g) The screen channel invert shall be 3 to 6
inches below the invert of the incoming sewers.
To prevent jetting action, the length and construction of the screen
channel shall provide for a reestablished hydraulic flow pattern following the
drop in elevation.
(h) The capacity of all screening equipment shall
be as follows:
(1) If one unit
is installed, the unit shall be sized to handle peak hourly design flow;
(2) If multiple
units are installed for flexibility of maintenance, the peak hourly design flow
shall be handled by the remaining units with the largest unit out of service;
and
(3) To avoid
excessive head loss and potential damage to very fine screens when very fine
screens are installed, multiple stages of screens with progressively smaller
openings shall be used.
(i) Influent channels
shall be equipped with gates to isolate each screening device. The channel preceding and following the
screen shall be shaped to eliminate settling of solids.
(j) Where a single mechanically-operated
screening device is used, auxiliary manually-cleaned screens shall be
provided. The design shall include
provisions for automatic diversion of the entire sewage flow through the
by-pass screen if the mechanical unit fails.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
709.03 Grit Removal Facilities.
(a) Grit removal facilities shall be provided for
all WWTPs for protection of downstream processes and equipment.
(b) If grit is removed by a means that causes the
grit to contain excess organics or water, or both, for the method of final grit
disposal to be used, the WWTP shall include grit washing and dewatering
facilities as necessary. Impervious
surfaces with drains shall be provided for grit handling areas. Grit conveying equipment shall be designed to
avoid loss of material and shall be protected from freezing. A pressurized water supply shall be provided
for cleanup.
(c) Where a single mechanically-operated grit
removal device is used, auxiliary manually-operated grit removal equipment
shall be provided. Design shall include
provisions for automatic diversion of the entire sewage flow through the
by-pass grit removal device should the mechanical unit fail.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
709.04 Grinding Facilities. Grinding devices may be used in addition to
screening devices if the following requirements are satisfied:
(a) Grinding devices installed in addition to
mechanical screening devices in a building where other equipment or offices are
located shall be separated from the rest of the building, provided with
separate outside entrances, and provided with mechanical ventilation; and
(b) Grinding devices that are installed in
addition to mechanical screening devices shall have slots no more than ¼-inch
wide and be designed to cut or shred material below the surface of the sewage.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 710
FLOW AND WASTE STRENGTH EQUALIZATION
Env-Wq
710.01 Flow and Waste Strength
Variations. If the WWTP is expected
to experience significant variations in organic or hydraulic loadings, the WWTP
shall incorporate methods and equipment to address the variations by either:
(a) Flow or waste strength equalization; or
(b) Alternate means that will ensure that the
WWTP operates effectively under the varying conditions.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
710.02 Equalization Tank: Location and Size.
(a) Equalization basins shall be located
downstream of pretreatment facilities such as mechanical screens, grinders, and
grit chambers.
(b) Equalization capacity shall be sufficient to
dampen expected flow and strength variations to the extent that is economically
advantageous or justified through a life cycle cost analysis.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
710.03 Equalization Tank: Aeration and Mixing.
(a) Aeration or mechanical mixing equipment shall
be provided to maintain adequate mixing, using corner fillets and hopper
bottoms with draw-offs to alleviate the accumulation of sludge and grit.
(b) Aeration equipment shall be provided to
maintain a minimum of 0.5 mg/L of dissolved oxygen in the mixed basin contents
at all times, with an air supply that is isolated from other WWTP aeration
requirements to facilitate process aeration control.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
710.04 Equalization Tank: Controls and Drainage.
(a) Inlets and outlets for all basin compartments
shall be suitably equipped with accessible external valves, stop plates, weirs,
or other devices to permit flow control and the removal of an individual unit
from service.
(b) Equalization tanks shall allow the entire tank
contents to be drained at a controlled rate and introduced to the remainder of
the treatment process.
(c) Facilities shall be provided to measure and
indicate liquid levels and flow rates.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 711
SETTLING
Env-Wq
711.01 Primary Settling Tanks.
(a) Inlets to primary settling tanks shall be
designed to:
(1) Dissipate
the inlet velocity in each tank to prevent short circuiting; and
(2) Distribute
the flow equally to multiple tanks.
(b) Channels in settling tanks shall be designed
to prevent sedimentation. Corner pockets
and dead ends are not permitted and shall be eliminated if they occur.
(c) Provisions shall be made for elimination or
removal of floating materials in inlet structures having submerged ports.
(d) The minimum length of flow from inlet to
outlet in rectangular settling tanks shall be 20 feet.
(e) Primary settling tanks shall have a minimum
side water depth of 12 feet.
(f) Effective scum collection and removal
facilities shall be provided ahead of the outlet weirs on all settling tanks.
(g) Overflow weirs shall be adjustable for
leveling.
(h) The tops of troughs, beams, and similar
construction features that are submerged shall have a minimum slope of 1.4
vertical to one horizontal.
(i) If primary
settling tanks are part of the WWTP design, a minimum of 2 primary settling
tanks shall be provided.
(j) All primary settling tanks shall provide safe
and easy access for maintenance and protection of operators. Access stairways and elevated walkways shall
be equipped with handrails. Walls of
primary settling tanks shall extend a minimum
of 6 inches above the surrounding ground surface, be provided with safety
railings, and have not less than 12 inches freeboard.
(k) For sludge removal from primary settling
tanks, provision shall be made for:
(1) Sampling
and measuring flow of the sludge; and
(2) For sludge
hoppers in rectangular settling tanks, a 1.7 horizontal to one vertical minimum
slope of the side walls.
(l) Settling tanks designed for use without
mechanical equipment for sludge collection and removal shall be prohibited.
(m) Air lift type of sludge removal shall be
prohibited. Primary sludge shall be
removed from the sludge hoppers by positive displacement pumps with timers for
control of pumping periods.
(n) Average surface overflow rates for primary
settling tanks shall not exceed 600 gpd per square foot (gpd/sf) for WWTPs
having an average design flow of 1 million gallons per day (MGD) or less.
(o) Average surface overflow rates for primary
settling tanks shall not exceed 1,200 gpd/sf for WWTPs having an average design
flow greater than 1 mgd, unless reduced primary
removal rates are provided in the design loadings for subsequent secondary
treatment units.
(p) Surface overflow rates for peak hourly flow
shall not exceed 3,000 gpd/sf.
(q) If activated sludge is wasted to the primary
tanks, average overflow rates shall not exceed 800 gpd/sf and peak hourly
overflow rate shall not exceed 1,200 gpd/sf.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
711.02 Secondary Settling Tanks:
Number and Types of Units.
(a) Multiple secondary settling tank units
capable of independent operation shall be provided.
(b) A minimum of 3 independent secondary settling
tanks shall be provided when the average daily
design flow is equal to or greater than 5.0 MGD.
(c) Secondary settling tanks for activated sludge
may be rectangular or circular, and shall be designed to separate and
concentrate mixed liquor, remove settled sludge, and skim, collect, and remove
scum and other floatables.
(d) Secondary settling tank walls shall:
(1) Extend at
least 6 inches above the surrounding ground; and
(2) Provide not
less than 12 inches of freeboard.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
711.03 Secondary Settling Tanks:
Design Criteria for Solids Loading.
(a) Secondary settling tanks shall be designed
integrally with the design of the aeration basins and sludge return
facilities. Secondary settling tank
sizing shall be based on solids loadings, sludge settleability, settled sludge
concentration, and return sludge rates.
(b) Solids loading shall be calculated as
follows:
(1) Peak solids
loading rate shall be computed based on the design mixed liquor suspended
solids (MLSS) under aeration and the design maximum daily flow rate plus the
corresponding recycle rate required to maintain the design MLSS;
(2) Allowable
solids loading rates shall be determined using solids flux analysis, expected
sludge characteristics, and a settling tank factor of safety of 1.3 to 1.5
times the maximum daily flow; and
(3) Settling
tank area shall be determined based on a solids flux analysis as specified in
section 6.3.5.4 of TR-16, “Guides for the Design of Wastewater Treatment Works”
by the New England Interstate Water Pollution Control Commission, revised 2016
edition, available as noted in Appendix B.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
711.04 Secondary Settling Tanks:
Design Criteria for Overflow Rates.
(a) Subject to (b), below, the design overflow
rates shall be determined from solids flux analysis and solids loadings.
(b) In lieu of (a), above, activated sludge
settling tanks treating domestic wastes may be sized according to Table 711-1
below, wherein overflow rates are based on solids flux with a factor of safety
of 1.3 against settling tank failure, overflow rates for systems with a
selector are based on settling characteristics typical of mixed liquor with a
sludge volume index (SVI) of 150 mL/g, and overflow rates for systems without
selectors are based on settling characteristics typical of a mixed liquor with
a SVI of 200 mL/g:
Table 711-1: Secondary Settling Tank Overflow Rates
Peak Hourly Flow
|
MLSS, mg/L |
Surface
Overflow Rates at Critical Loading with SVI = 150 mL/g, gpd/sf |
Surface
Overflow Rates at Critical Loading with SVI = 250 mL/g, gpd/sf |
|
1,500 |
2,100 |
1,850 |
|
2,000 |
1,710 |
1,450 |
|
2,500 |
1,400 |
1,140 |
|
3,000 |
1,140 |
900 |
|
3,500 |
930 |
690 |
|
4,000 |
760 |
550 |
|
4,500 |
610 |
440 |
|
5,000 |
510 |
340 |
(c) Side water depth for secondary settling tanks
shall be as follows:
(1) For
rectangular units, 12 to 13 feet;
(2) For
circular units up to 40 feet in diameter, 12 feet;
(3) For
circular units 40 feet to 75 feet in diameter, 14 feet;
(4) For
circular units 75 feet to 125 feet in diameter, 16 feet; and
(5) For
circular units greater than 125 feet in diameter, 18 feet.
(d) Circular settling tanks shall have a minimum
bottom slope of 0.25 inches per foot.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
711.05 Secondary Settling Tanks:
Design Criteria for Inlets and Outlets.
(a) Inlets shall be designed to minimize
short-circuiting and to distribute flow across the entire settling tank.
(b) Scum gathering in the inlet area shall be
minimized.
(c) V-notch weirs shall be provided for all
outlets. Head over the base of the
V-notch shall be less than the depth of the notch. Weirs shall be adjustable to correct for any
differential settlement of the tanks.
(d)
Effluent launders shall be designed to convey the maximum instantaneous flow
without surcharging.
(e) Launder inverts shall be sloped a minimum of
0.5 percent.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
711.06 Secondary Settling Tanks:
Design Criteria for Sludge and Scum Removal.
(a) Sludge collection and withdrawal facilities
shall be designed to accommodate the withdrawal of sludge solids.
(b) Circular units shall be designed to allow
alternate sludge wasting and tank drainage from the center of the units.
(c) Rapid sludge removal systems in circular
settling tanks shall be designed so that return rates can be directly varied by
changes in return sludge pumping rates.
Sludge collection tubes on rapid sludge removal systems shall have a
submerged discharge to the center well.
(d) Chain and flight sludge collectors in
rectangular settling tanks shall be designed with a minimum horizontal velocity
of 2 to 3 feet per minute with flights at least 10 feet on center.
(e) Effective baffling to prevent velocity and
density currents within the tank and scum removal equipment shall be provided
in each secondary settling tank. Scum
removal equipment shall facilitate the positive movement of scum to the scum
hoppers.
(f) Scum hoppers shall have provisions to
facilitate the flushing of scum from the hopper.
(g) Scum piping shall be sized for proper
movement of viscous foams.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
711.07 Secondary Settling Tanks:
Design Criteria for Return Sludge.
(a) Return sludge rate capabilities shall be
designed to be the greater of 100 percent of maximum month design flow or 150
percent of annual average day design flow.
(b) At least one return sludge pumping unit shall
be provided for each settling tank. The
maximum required return sludge capacity shall be available with the largest
pumping unit out of service. Pumps may
be placed on suction headers, but the arrangement and valving shall be such
that any one settling tank can be isolated with a single pump.
(c) A positive suction head shall be provided for
all return sludge pumps.
(d) Return sludge pumps shall have at least
3-inch suction and discharge openings.
(e) Rate of sludge return shall be varied by
means of variable speed motors, drives, or timers.
(f) Return sludge suction and discharge piping
shall be at least 4 inches in diameter and designed to maintain a velocity of
not less than 2 feet per second when operating at average sludge return rates.
(g) Suitable devices shall be provided for
sampling and measuring return sludge flow rates. Measuring devices shall totalize and record,
as well as indicate flows.
(h) Capability shall be provided to return and
waste sludge concurrently.
(i) Provisions shall
be made for the draining and flushing of discharge lines.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
711.08 Secondary Settling Tanks:
Design Criteria for Waste Sludge.
(a) Means for measuring, sampling, and
controlling the rate of waste activated sludge flow shall be provided. Measuring devices shall totalize and record,
as well as indicate flows.
(b) Waste sludge shall be discharged to primary
settling tanks, units for concentrating the waste sludge, storage tanks,
digesters, dewatering devices, or to other means of direct removal from the
plant.
(c) Waste sludge facilities shall be designed to
pump the expected minimum and maximum rates of wasting.
(d) Provisions shall be made for the draining and
flushing of discharge lines.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 712
CHEMICAL COAGULATION FOR PRIMARY AND SECONDARY SETTLING TANKS
Env-Wq
712.01 Chemical Coagulation:
Application and Mixing.
(a) Chemical coagulants shall be applied at a
rate proportional to the wastewater flow.
(b) Rapid and thorough mixing of the wastewater
and coagulant(s) shall be provided in small tanks or pipes using:
(1) Inline
blenders;
(2) Air mixers;
(3) Mechanical
mixers; or
(4) Baffles.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
712.02 Chemical Coagulation: Flocculation Tanks.
(a) Flocculation following chemical coagulant
mixing shall be completed in channels or tanks that meet the following
requirements:
(1) At least 2
flocculation tanks or channels having a combined detention period of between 20
and 30 minutes shall be provided;
(2) Mixing
shall be balanced to avoid under-mixing or over mixing such that:
a. Chemicals
are completely dispersed;
b. Flocculated
particles do not settle; and
c. Flocculated
particles are not sheared; and
(3) Independent
controls for each tank shall be provided.
(b) Settling tank design shall conform to Env-Wq
711.
(c) A means of dewatering all tanks shall be
provided.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
712.03 Chemical Coagulation: Process
Impacts. Chemical coagulation shall
not be used unless the owner first evaluates the following potential impacts
due to chemical addition:
(a) Increased sludge production;
(b) Change in sludge thickening and dewatering
characteristics;
(c) Biological phosphorous removal and
denitrification capability;
(d) Sludge settling characteristics in subsequent
treatment processes; and
(e) Increased operation and maintenance costs of
the chemical feed system.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 713
SUSPENDED GROWTH BIOLOGICAL TREATMENT
Env-Wq
713.01 Activated Sludge: General
Design Requirements.
(a) The activated sludge process and its various
modifications shall be used only where sewage is amenable to biological
treatment.
(b) WWTP design shall provide for multiple
aeration tanks capable of passing peak hourly flow with one unit out of service
and of meeting process requirements with all units on line.
(c) Where the WWTP design provides for all return
sludge to be mixed with the raw sewage or primary effluent at one location,
then the mixed liquor flow rate to each aeration unit shall be equal by means
of a controlled distribution structure.
(d) All activated sludge designs shall include
provisions for the control of bulking sludge and filamentous micro-organisms.
(e) Return sludge equipment shall comply with the
following:
(1) The return
sludge rate shall be varied by means of variable speed motors, drives, or
timers. All designs shall provide for
flexibility in operation. The return
sludge rate shall be at least 100 percent of average annual influent design
flow and sufficient to maintain design MLSS at maximum day flow rates;
(2) The maximum
return sludge capacity shall be obtained with the largest pump out of service;
and
(3) A method
for observing, sampling, and controlling return activated sludge flow from each
settling tank shall be provided.
(f) Waste sludge facilities shall comply with the
following:
(1) In addition
to capacity required for return sludge pumping, waste sludge pumping facilities
shall be provided with a minimum capacity not less than 25 percent of design
average rate of wastewater flow, or a minimum of 10 gpm,
whichever is larger. Waste sludge pumps
shall function satisfactorily at 0.5 percent of design annual average
wastewater flow;
(2) Waste
activated sludge may be discharged to the primary settling tanks, sludge
digestion tanks, sludge thickening or dewatering processes, storage tank or any
practical combination of these units; and
(3) A method
for observing, sampling, and controlling waste activated sludge flow shall be provided.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.02 Activated Sludge: Aeration
System Requirements.
(a) An aeration system shall be designed to:
(1) Meet
maximum oxygen demand and mixing requirements and maintain process performance
with the largest unit out of service;
(2) Provide for
varying the amount of oxygen transferred in proportion to the load demand on
the WWTP; and
(3) Have
motors, gear housing, bearings, grease fittings, and other parts requiring
maintenance in a location that is:
a. Accessible
under routine operating conditions; and
b. Protected
from submergence and spray as necessary for proper functioning.
(b) The mechanism and drive unit for oxygen
transfer shall be:
(1) Designed
for the expected conditions in the aeration tank in terms of power performance;
and
(2) Tested and
certified by the aerator manufacturer.
(c) Each aeration drop leg shall be equipped
with:
(1) Control
valves that have indicator markings for throttling and complete shut off; and
(2) Air flow
measurement capability.
(d) Air filters shall be:
(1) Provided in
numbers, arrangement, and capacities to furnish at all times an air supply
sufficiently free from dust to prevent damage to blowers and clogging of the
diffuser system used; and
(2) Equipped
with a means to measure pressure drop across the air filters.
(e) Blowers shall be located in a room that:
(1) Is
separated from the office, laboratory, or control room by insulated walls to
minimize blower noise, such that the noise level does not exceed 90 decibels in
the blower room and does not exceed 50 decibels in the office, laboratory, or
control room;
(2) Has
mechanical ventilation; and
(3) Is equipped
with heat recovery units if economically justified based on life cycle cost
analysis.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.03 Activated Sludge: Aeration
System Performance Requirements.
(a) To allow for increased energy efficiency in
WWTP
operation through the expected life of a WWTP, the owner shall:
(1) Provide
multiple blowers for diffused air systems that are sized to:
a. Meet the
current facility peak aeration demand;
b. Meet
turndown requirements as described in (b), below; and
c. Avoid
over-aerating at current daily minimum flows;
(2) Conduct an
energy evaluation to determine the optimum blower sizing, turndown, and
staging;
(3) If current
peak aeration demands are below peak design aeration demands, provide
sufficient blower capacity to meet current peak aeration demands while ensuring
that blower rooms are large enough to accommodate the blower configuration
necessary to meet peak design demands;
(4) Demonstrate
financial capacity or set up a reserve account to set aside the estimated money
required to install additional blowers when needed to meet increased peak
aeration demands; and
(5) Arrange
blowers in such configuration and capacities as to meet the current peak
aeration demands with the single largest unit out of service.
(b) The aeration system shall be designed to:
(1) Have
sufficient turndown capability that does not extend beyond the efficient
operational range of the blowers, when using multiple same-sized blowers or
staging with multiple varied-sized blowers;
(2) Not
over-aerate or require blowing off excess air at initial year minimum flows;
and
(3) Operate
most efficiently at average organic loading conditions.
(c) Air requirements for a diffused air system
shall be determined by incorporating the following factors, which shall be included in the design
specifications or supporting documentation submitted to the department:
(1) Tank depth;
(2) Alpha
factor of waste;
(3) Beta factor
of waste;
(4) Certified
aeration device transfer efficiency;
(5) Minimum
aeration tank dissolved oxygen concentration;
(6) Mixing
requirements needed to maintain solids suspension;
(7) Critical
wastewater temperature; and
(8) Altitude of
WWTP.
(d) Aeration requirements for carbonaceous BOD5
removal shall be based upon the maximum monthly BOD5 loading.
(e) All aeration equipment shall be capable of
maintaining a minimum of 1.0 mg/L of dissolved oxygen in the mixed liquor
unless a lower minimum dissolved oxygen can be justified based on process
modeling.
(f) Diffused air system design shall use data
derived from pilot testing or an empirical approach.
(g) When pilot facility or experimental data is
not available, the design oxygen requirements shall:
(1) Be 0.8 to
1.2 pounds of oxygen per pound BOD5 removed;
(2) Be 4.57
pounds oxygen per pound design maximum day total Kjeldahl nitrogen (TKN)
available for nitrification, where TKN available for nitrification is
calculated as influent TKN less nitrogen required for carbonaceous growth less
non-biodegradable nitrogen; and
(3) Include
oxygen demands due to high BOD5 and TKN concentrations in recycle
flows such as heat treatment and digester supernatants, vacuum filtrate, belt
filter pressate, waste sludge recycled to primary
clarifiers, and elutriates.
(h) The aeration system shall be designed to
match the diurnal organic load variation while economizing on power input.
(i) The capacity of
the blowers or air compressors shall be based on the site altitude and site
specific minimum and maximum summer and winter temperatures.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq
713.04 Activated Sludge: Protection
of Aeration Systems.
(a) Electrical controls for all aeration
equipment shall be protected from the elements.
(b) Where extended cold weather conditions occur,
the aerator mechanism and associated structure shall be protected from freezing
due to ice formation from splashing.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.05 Activated Sludge: Aeration
Tank Design.
(a) The aeration tank size for any particular
adaptation of the activated sludge process shall be determined by:
(1) Pilot
studies; or
(2) Rational
calculations based primarily on solids retention time (SRT) and MLSS levels
while also considering other factors, including but not limited to capacity,
wastewater characterization relevant to the proposed process, diurnal load
variations, degree of treatment required, pH, temperature, alkalinity, and
dissolved oxygen.
(b) The engineer shall furnish aeration tank
sizing calculations to the department with the engineering design documents.
(c) Aeration tank volume requirements for
nitrification shall be based on maximum monthly loading.
(d) The dimensions of each independent mixed
liquor aeration tank or return sludge re-aeration tank shall be such as to
maintain effective mixing and use of air, provided that liquid depths shall be
not less than 12 feet nor more than 25 feet.
(e) Inlets and outlets for each aeration tank
unit shall be equipped with valves, gates, stop plates, weirs, or other devices
to permit flow control to any unit and to maintain a constant liquid level
while preventing short-circuiting through the tank.
(f) Channels and pipes carrying liquids with
solids in suspension shall be designed to maintain self-cleansing velocities or
shall be agitated to keep such solids in suspension at all rates of flow within
the design limits.
(g) Piping shall allow flexible operation
sequence of tanks and returned sludge inlets.
(h) Aeration tank freeboard shall be:
(1) Not less
than 3 feet if a mechanical surface aerator is used; and
(2) Not less
than 18 inches in all other aeration tanks.
(i) Froth and foam
control or removal shall be provided at the aeration tanks.
(j) Thorough mixing of the mixed liquor to
prevent deposition of solids at any point in the tanks shall be provided.
(k) Aeration tanks shall have probes to monitor
dissolved oxygen in place, to control power consumption, and match oxygen demand with oxygen
supply.
(l) Diffusers shall be spaced to satisfy
oxygenation requirements through the length of the channel or tank, and to
facilitate spacing adjustments without major revisions to the existing air
header piping.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq
713.06 Oxidation Ditches.
(a) Oxidation ditch design shall be based on
experience at other comparable facilities and meet the applicable requirements
of Env-Wq 713.01 through Env-Wq 713.05 except as modified in this section.
(b) Oxidation ditch design shall comply with the
following requirements:
(1) Ditches
shall be interconnected such that either ditch can be taken out of service
temporarily and the ditches can be operated either in series or in parallel;
and
(2) Minimum
horizontal velocity shall be not less than one foot per second.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
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Env-Wq
713.07 Sequencing Batch Reactors.
(a) Sequencing batch reactor (SBR) design shall
be based on experience at comparable facilities and meet the applicable
requirements of Env-Wq 713.01 through Env-Wq 713.05 except as modified in this
section.
(b) SBRs shall be designed and constructed to
allow for static fill, mixed fill, and aerated fill to allow for operational
flexibility.
(c) More than 2 tanks shall be provided, unless
one of the following is provided:
(1) An influent
flow equalization tank sized to hold a minimum of 2 design capacity decantable
volumes; or
(2) Provisions
to allow SBR tanks to operate in a continuous flow-through mode during
emergency operations.
(d) System sizing shall be based on aerated SRT.
(e) System reliability with any single SBR tank
out of service and the instantaneous flow delivery shall be evaluated in the
design of decanter weirs and approach velocities.
(f) The decanter shall not create a vortex or
take in floatables or sludge.
(g) Scum removal shall be provided.
(h) The SBR design shall include in-place
dewatering capability and provisions for transferring mixed liquor between the
SBR tanks.
(i) Each SBR tank
shall be capable of wasting sludge during each cycle.
(j) If blowers are provided, blowers shall meet
the requirements of Env-Wq 713.02
through 713.05.
(k) Mechanical mixing independent of aeration
shall be provided for all systems where biological phosphorous removal or
denitrification is required, with mixing equipment sized to thoroughly mix the
entire basin from a settled condition within 3 minutes without aeration.
(l) Post-SBR tank flow equalization shall be
provided to equalize flow variations and designed to meet the following
criteria:
(1) Hold a
minimum of one design capacity decantable volume;
(2) Provide a
means to return the decanted effluent to the headworks for additional
treatment; and
(3) Provide a
means to remove solids from the tank bottom.
(m) An automatic process control having an
uninterruptible power supply with electrical surge protection shall be
provided.
(n) Manual override shall be provided in addition
to automatic process control. Both
automatic and manual controls shall allow independent operation of each tank.
(o) Controls shall allow at least 20 minutes of
settling between the react and decant phases.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.08 Aerated Lagoon Design: General
Requirements.
(a) To develop final design parameters for
aerated lagoons, actual operating data shall be used, if available.
(b) If actual data is not available, the aerated
lagoon system design for minimum detention time in days (t) shall be estimated
for each aerated cell by dividing the percent of BOD5 to be removed
in the aerated lagoon (E) by the product of 2.3 multiplied by the reaction rate
coefficient for an aerated lagoon in base 10 (k1) multiplied by the
result of subtracting E from 100, as shown in the following formula:
t =
E
2.3k1(100-E)
(c) For purposes of (b), above, the reaction rate
coefficient (k1) shall be as follows:
(1) For
domestic wastewater, 0.12/day at 68°F, equivalent to 20°C, and 0.06/day at
34°F, equivalent to 1°C, unless data is available to indicate a more
appropriate k1 value for the specific site;
(2) For
domestic wastewater that includes some industrial wastes, other wastes, and
partially treated wastewater, as determined experimentally for various
conditions which might be encountered in the aerated ponds; and
(3) Conversion
of the reaction rate coefficient to other temperatures shall be made based on
experimental data.
(d) There shall be a minimum of 3 separate
cells. Baffles may be used to create up
to 2 cells in one lagoon.
(e) All aerated lagoon systems shall be designed
with piping flexibility to allow isolation of any cell without affecting the
transfer and discharge capabilities of the total system.
(f) The ability to discharge influent waste load
to a minimum of 2 cells or all primary cells in the system shall be provided.
(g) The shape of all lagoons shall be such that
there are no narrow or elongated portions.
Lagoons shall be round, square, trapezoidal, or rectangular with the
length not exceeding 3 times the width.
(h) Additional lagoon volume of at least 20
percent shall be included for sludge storage and ice cover.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.09 Aerated Lagoon Design:
Aeration Equipment. In addition to
the applicable portions of Env-Wq 713.02 through Env-Wq 713.05, aerated lagoon
aeration equipment shall meet the following requirements:
(a) Aeration shall be of the diffused or
mechanical mixing type; and
(b) For diffused air systems:
(1) Multiple
blower units shall be provided and sized such that, with any unit out of
service, the remaining units are capable of supplying all aeration needs;
(2) Means shall
be provided for regulating, measuring, and recording the flow of air to the
lagoons;
(3) Air
diffusion piping headers and piping supports shall be corrosion-resistant with
a durability for the anticipated life of the WWTP; and
(4) Ductile
iron pipe headers or piping shall not be cement lined.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.10 Aerated Lagoon Design: Inlet
and Outlet Piping.
(a) Aerated lagoon piping systems shall be
designed to avoid areas of stagnation, short circuiting, solids deposition, or
dead zones in the lagoons.
(b) Inlet piping shall be located 1/5 to 1/3 of
the total water depth from the lagoon bottom, but not less than 2 feet above
the bottom of the lagoon bottom. On
lagoons 150 or more feet wide, multiple inlets shall be used to enhance
distribution of the influent flow.
(c) Outlets shall be designed to provide multiple
draw-off levels. Draw-off capability
shall be provided over as much of the operating depth as feasible.
(d) All aerated cells shall have influent lines
which distribute the load within the mixing zone of the aeration equipment to
minimize short-circuiting.
(e) The influent line shall discharge vertically
on to a concrete apron no smaller than 4 square feet to prevent scouring and
erosion.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.11 Aerated Lagoon Design:
Distribution and Interconnection Piping.
(a) Self-cleaning velocities shall be present in
aerated lagoon distribution piping.
(b) To prevent erosion due to discharge at the
termination of distribution and interconnecting piping, the piping shall
discharge vertically on a concrete apron 4 feet square, as a minimum.
(c) Interconnecting piping shall discharge
vertically near the lagoon bottom and at the dike, thereby reducing erosion
effects.
(d) Piping shall be ductile iron, stainless
steel, HDPE, or SDR 35 PVC.
(e) Distribution and interconnection piping
clean-outs shall be provided.
(f) Seepage collars shall be provided around any
pipes penetrating the dike. The collars
shall extend a minimum of 2 feet radially from the pipe.
(g) Flow distribution structures shall be
designed to effectively split hydraulic and organic loads equally to primary
cells.
(h) All primary cells shall have individual
influent lines that terminate approximately at the mid-point of the cell width
and at approximately 2/3 of the cell length away from the outlet structure to
minimize short-circuiting.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.12 Aerated Lagoon Design:
Overflow Structures.
(a) Intakes for aerated lagoon overflow
structures shall be located a minimum of 10 feet from the toe of the dike and 2
feet below the top of the liner.
(b) Weirs or gates shall be of lightweight,
corrosion-resistant material such as aluminum or fiberglass.
(c) Scum baffle mechanisms shall be provided.
(d) Provision shall be made for draining the
lagoons.
(e) Location of draw off pipes shall minimize
erosion effects.
(f) To prevent overtopping the dikes, emergency
overflow between cells shall be provided.
(g) Hydraulic capacity for discharge structures
and piping shall allow for a minimum of 250 percent of the design maximum day
flow of the system.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.13 Aerated Lagoon Design:
Embankments, Dikes, and Bottom.
(a) Aerated lagoon dikes, embankments, and
bottoms shall form a stable structure impervious to seepage of lagoon liquid.
(b) The minimum top width of a dike or embankment
shall be 8 feet to permit access by maintenance vehicles.
(c) Aerated lagoon dikes and embankments shall
have inner faces not steeper than a 3:1 slope nor shallower than a 4:1 slope,
and outer faces not steeper than a 3:1 slope.
(d) Aerated lagoons shall be designed such that
surface water shall not flow or drain into the lagoons.
(e) Aerated lagoon dikes shall be designed to
provide a minimum of 3 feet of freeboard above normal lagoon water surface
elevation.
(f) For aerated lagoon systems, the design water
depth shall range from a minimum of 10 feet to a maximum of 20 feet.
(g) Seeding and erosion control shall be as
follows:
(1) Outside
slopes shall be seeded with perennial type, slow growing, spreading grasses
that minimize erosion and can be mowed; and
(2) Inside
slopes shall have rip rap or comparable material of suitable size and weight
installed from the top of the dike to at least one foot below normal lagoon
operating level to protect the slopes from erosion and wave action.
(h) The lagoon bottom shall be smooth and level
at all points. Finished elevations shall
vary not more than 3 inches from the average elevation of the bottom.
(i) A minimum
separation of 4 feet between the bottom of the pond and the maximum ground
water elevation shall be provided unless an effective underdrain system is
provided.
(j) A minimum separation of 2 feet between the
liner bottom at the bottom of the lagoon and any bedrock formation shall be
provided.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.14 Aerated Lagoon Design:
Groundwater Pollution and Soil Formation.
(a) Contamination of groundwater by transmission
through the soil or overflows that can cause a health hazard in water supplies
or cause ground or surface water quality violations shall be prohibited.
(b) Liquid loss through the lagoon dikes and
bottom shall be prohibited.
(c) Impervious membrane liners shall be installed
in all new lagoons.
(d) Lined lagoons shall be permitted as required
by Env-Or 700.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
713.15 Aerated Lagoon Design: Area
Control.
(a) Fencing shall surround the entire site with
locking access gates for vehicles and equipment. Fencing shall not obstruct maintenance
vehicle traffic on top of the dikes.
(b) An all-weather access road shall be provided
to the pond site to allow year-round maintenance of the facility.
(c) Warning signs advising against trespassing
and showing the nature of the facility shall be posted along the fence as
follows:
(1) At least
one sign on each side of the site; and
(2) At least
one sign for every 500 feet of the fence’s perimeter.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 714
FIXED FILM BIOLOGICAL TREATMENT
Env-Wq
714.01 Trickling Filters: General
Requirements.
(a) Biological trickling filters shall only be
used when the sewage is amenable to treatment by aerobic biologic processes.
(b) Trickling filters shall be preceded by
effective settling tanks equipped with scum collecting devices or other
suitable pretreatment facilities and followed by secondary settling tanks in
accordance with Env-Wq 711.02 through Env-Wq 711.08.
(c) Trickling filters shall be designed either as
low-rate or high-rate filters which incorporate recirculation. Reduction in BOD5 in primary
settling tanks shall not exceed 35 percent for filter design criteria.
(d) Design submittal requirements shall be as
specified in Env-Wq 703.
(e) WWTP design shall provide for multiple
trickling filters capable of passing peak hourly flow with one unit out of
service and of meeting process requirements with all units on line.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
714.02 Trickling Filters: Size
Requirements.
(a) Trickling filters treating domestic wastes
shall be sized according to Table 714-1 below, subject to the notes in (b) below:
Table 714-1:
Trickling Filter Design Criteria
|
Design
Parameter |
Roughing |
Carbon
Oxidizing (cBOD5 removal) |
cBOD5
and Nitrification |
Nitrification |
|
Media typically used |
Vertical Flow |
Rock, cross-flow or vertical flow |
Rock, cross-flow or vertical flow |
Cross-flow |
|
Media-specific surface area, sf/cf |
31 to 40 |
14 to 68 |
14 to 68 |
30 to 68 |
|
Wastewater Source |
Primary effluent |
Primary effluent |
Primary effluent |
Secondary effluent |
|
Hydraulic loading, gpm/sf |
0.9 to 2.9 |
0.25 to 1.5 |
0.25 to 1.5 |
0.6 to 1.5 |
|
Lb BOD5/d-1000 cf |
100 to 220 |
20 to 60 |
5 to 15 |
not applicable |
|
Lb NH3 -N/d-1000 cf |
not applicable |
not applicable |
0.04 to 0.2 |
0.1 to 1.5 |
|
Effluent quality, mg/L unless noted |
50 to 75% filtered cBOD5 conversion |
15 to 30 cBOD5 and TSS |
<10 cBOD5 <3 NH3 –N A |
0.5 to 3 NH3 –N |
|
Predation |
No appreciable growth |
Beneficial |
Detrimental (nitrifying biofilm) |
Detrimental |
|
Filter flies |
No appreciable growth |
No appreciable growth |
No appreciable growth |
No appreciable growth |
|
Depth |
3 to 20 |
5 to 40 |
5 to 40 |
5 to 40 |
(b) In Table 714-1, the letter “A” means the
concentration remaining in the clarifier effluent stream.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
714.03 Rotating Biological Contactors
(RBCs).
(a) Rotating biological contactors (RBCs) shall
only be used when the sewage is amenable to treatment by aerobic biological
processes.
(b) RBC units shall be housed or otherwise
protected from winter conditions, freezing damage, and UV degradation.
(c) Covers shall be designed to provide adequate
ventilation and enclosed structures shall be protected from corrosion due to
high humidity. Enclosures shall allow
for the removal of one shaft without interfering with the WWTP operation.
(d) Covers shall allow operator access to all
parts of the RBCs for observation and maintenance.
(e) RBCs shall be preceded by effective settling
tanks equipped with scum collecting devices or other suitable pretreatment
facilities in addition to those required in Env-Wq 711.01.
(f) Multiple trains shall be furnished for
flexible operation and stage bypassing.
(g) Flow control to RBC tanks shall be by
splitter boxes and weirs.
(h) Buildings housing RBC processes shall have
ventilation of at least 6 air changes per hour.
(i) Electrical system
components, panels, light fixtures, motors, and control centers shall be
watertight and corrosion resistant.
(j) Shafts and media shall be designed for an
operational life of 20 years.
(k) RBC units shall be sized in accordance with
the following:
(1) Organic
loading to the first stage of the RBC system shall not exceed 6 to 8 pounds of
BOD5/1,000 square feet/day or 2.5 to 4 pounds of soluble BOD5/1,000 cubic
feet/day; and
(2) Maximum
bearing capacities for the shafts shall be specified based on the expected film
thickness, the capacity to strip biofilm, and an adequate margin of
safety. Load cells shall be provided for
all shafts to monitor loadings.
(l) Media shall be constructed to allow portions
to be removed for cleaning and replacement without requiring the entire shaft
assembly to be removed from the tanks.
(m) Adequate flexibility in process operation
shall be provided by including one or more of the following in the design:
(1) Variable
rotational speeds in the first and second stages, including speed reversal to
remove excess biofilm;
(2) Removable
baffles between all stages in contoured basins to avoid dead spaces;
(3) Positive
influent flow control to each unit or flow train, including
positively-controlled alternate flow distribution systems such as step feed;
(4) Positive
air flow metering and control to each shaft when supplemental air or motor
driven units are used; or
(5)
Recirculation of secondary effluent.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 715
DISINFECTION
Env-Wq
715.01 Disinfection Requirement. All wastewater shall be disinfected prior to
discharge when the discharge permit includes bacteria limitations.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
715.02 Methods. The following disinfectant methods shall be
allowed for wastewater discharges:
(a) Sodium hypochlorite or calcium hypochlorite;
(b) Ultraviolet irradiation; or
(c) Other performance-based innovative
technologies that are shown to be cost-effective and able to meet the
disinfection requirements of the discharge permit.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
715.03 Hypochlorite Systems.
(a) Hypochlorite solution feed equipment shall
incorporate effluent flow proportional control systems or effluent flow
proportional combined with demand proportional control systems.
(b) Hypochlorite feeders shall be of the positive
displacement type.
(c) Hypochlorite solution storage shall be of
sufficient volume to provide for dosing at the anticipated maximum dose rate at
design annual average flow for 15 days.
(d) Hypochlorite solution feed systems shall be
capable of dosing at the anticipated maximum dose rate at maximum flows, with
turndown capabilities to accommodate minimum flows.
(e) A redundant hypochlorite feed pump shall be
provided.
(f) Rooms housing hypochlorite feed equipment and
appurtenances shall be mechanically ventilated to provide at least 6 air
changes per hour.
(g) Mechanical ventilation systems shall draw
from floor level.
(h) Application of hypochlorite shall be as
follows:
(1) Mixing of
the disinfectant at the point of injection before the contact tank shall be
provided using hydraulic or mechanical means; and
(2) A minimum
contact period of 15 minutes at peak hourly flow or maximum rate of pumping
shall be provided.
(i) Contact tank
design shall be as follows:
(1) The contact
tank shall have a minimum of 2 separate chambers;
(2) The contact
tank shall be configured to reduce short-circuiting of flows;
(3) A minimum
40:1 length to width ratio of the contact passage shall be provided;
(4) A scum
baffle and scum removal piping shall be provided at the effluent end of the
tank;
(5) Provisions
shall be made for draining and washing down the contact tank; and
(6) Drainage
flow shall be returned to the treatment process.
(j) Facilities shall be provided for obtaining
samples, either grab or continuous as stipulated by permit, of the disinfected
effluent after contact.
(k) Equipment for residual chlorine testing and
recording shall be provided, which is capable of measuring in the range from 10
parts per million to the lower limit established by permit.
(l) Alarm systems shall be provided for:
(1) Low
hypochlorite storage tank level;
(2) High
hypochlorite storage tank level; and
(3) Failure of
the hypochlorite feed system.
(m) Hypochlorite solution, storage tanks, pumps, and feed
lines shall be protected from freezing.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
715.04 Dechlorination
Systems.
(a) Dechlorination to
reduce free and combined chlorine residuals in WWTP effluent, if required by
permit, shall be by use of sulfite salt solutions.
(b) Dechlorination
systems shall:
(1) Be sized to
chemically neutralize 5 parts per million total residual chlorine at all flows;
(2) Be of the
positive displacement type;
(3) Include
storage of sufficient volume to provide for dosing at the anticipated maximum
dose rate at design annual average flow for 15 days;
(4) Include a
redundant dechlorination feed pump;
(5) Provide
thorough hydraulic or mechanical mixing at the point of sulfite injection;
(6) Provide a
flow proportional feed forward control system;
(7) Provide a
sampling point for compliance monitoring after dechlorination;
(8) Provide an
alarm system to actuate upon failure of the dechlorination
feed system;
(9) Have
chemical storage tanks equipped with a mechanical mixing device to keep the
chemical solution completely mixed; and
(10) Have dechlorination solutions, storage tanks, pumps, and feed
lines protected from freezing.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
715.05 Ultraviolet (UV) Irradiation
Systems.
(a) An initial assessment of the capabilities of
UV disinfection shall be made through transmittance testing to demonstrate the
absence of interfering constituents.
(b) UV disinfection systems shall deliver UV
radiation dosages as demonstrated by plant-specific pilot testing to be
effective in maintaining compliance with the bacteriological limits of the
discharge permit.
(c) The UV disinfection system shall consist of
multiple banks of lamp modules capable of disinfecting peak hourly flows with
one bank out of service.
(d) Provisions shall be made for easy removal and
inspection of UV lamps for maintenance or replacement without draining the UV
channel.
(e) Provisions shall be made for cleaning the
lamp sleeves.
(f) Provisions shall be made for draining and
cleaning the UV channel while maintaining adequate disinfection or storing
forward flow.
(g) For facilities with a design average flow in
excess of 100,000 gpd, UV system controls shall enable UV disinfection system
output to be varied in proportion to the effluent flow, percent transmittance,
or a combination of both parameters in order to disinfect over the range of
water quality conditions.
(h) Warning alarms and automatic shutdown shall
be provided. Lamp output through the
contact area shall be monitored, and a low dosage warning signal shall be
furnished.
(i) The UV system
shall be connected to the WWTP’s standby power source and shall be equipped
with an uninterruptible power supply to power unit during transfers to and from
the standby power source.
(j) The UV system shall not produce any dangerous
levels of ozone.
(k) The UV system operating area shall be
ventilated.
(l) The UV system shall be fully enclosed in a
building for year-round operation.
(m) Provisions for measuring UV transmittance
shall be provided.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 716
SLUDGE HANDLING AND DISPOSAL
Env-Wq
716.01 Sludge Stabilization Methods.
(a) Liquid or solid phase sludge stabilization in
accordance with this part shall be required prior to the beneficial use of
sludge and scum in accordance with Env-Wq 800 and 40 CFR Part 503.
(b) Acceptable solid phase sludge stabilization
processes after dewatering shall be based on the types and quantities of
wastewater, septage, and other waste streams to be accepted, as applicable, and
may include one or more of the following:
(1) Composting;
(2) Heat
drying;
(3)
Pasteurization;
(4) Air-drying;
and
(5) Lime
stabilization.
(c) Acceptable liquid phase sludge stabilization
processes shall be as follows:
(1) Anaerobic
digestion, including mesophilic and thermophilic processes;
(2) Aerobic
digestion;
(3) Liquid lime
stabilization; and
(4) Other
processes approved under Env-Wq 800 and 40 CFR Part 503.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.02 Sludge Stabilization Design
Requirements.
(a) Sludge stabilization processes shall be
designed to meet the requirements of Env-Wq 800 for pathogen and vector
attraction reduction for Class A or Class B biosolids.
(b) Proprietary processes for which design
criteria are primarily provided by equipment manufacturers to accommodate their
equipment and design concepts shall be supported by a detailed basis of design
which cites existing successfully-operating facilities with similar solids
types and similar capacities with similar design criteria.
(c) Access for maintenance, repair, and
inspection shall be provided for all stabilization process equipment and
related tankage.
(d) Safety devices shall include:
(1) Automatic
shutdown upon critical system component malfunction;
(2) Alarm
systems for equipment failure; and
(3) Alarm
systems for hazardous conditions.
(e) Redundancy of equipment and tankage or
storage shall be provided so that the solids stabilization process will
continue to be operable in the event of a failure of any single system
component.
(f) Odor control technology and practices shall
be provided to control odors generated from the solids handling processes to
minimize the impact of odors outside the facility property boundaries.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.03 Sludge Handling and Disposal
Design Criteria. A complete summary
of the proposed design criteria for solids handling processes shall be provided
in the basis of design, including:
(a) Intended disposal methods;
(b) Projected design year loadings;
(c) A detailed description and analysis of the
design criteria used to select an alternative design, if applicable;
(d) Projected performance; and
(e) Proposed odor control technology.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.04 Sludge Grinder Pumps.
(a) Sludge grinder pumps shall be installed prior
to sludge processing equipment that would be adversely affected by large
solids.
(b) Grinders shall be installed on the suction
side of the pump to prevent clogging.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.05 Sludge Storage Requirements.
(a) Sludge storage facilities shall be designed
to control odors so that odors do not create a nuisance at the property
boundary.
(b) Storage capacity shall be designed to
accommodate at least 5 days of sludge production based on maximum month design
sludge generation rate.
(c) Storage areas shall be designed to minimize
tracking of dewatered cake on-site and eliminate runoff from the dewatered cake
storage area to other portions of the site or off-site.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.06 Anaerobic Sludge Digestion:
Tanks.
(a) Multiple tanks piped to operate both in
series and in parallel shall be provided for the anaerobic sludge digestion
process unless alternate methods of sludge stabilization and emergency storage
are provided.
(b) Tank capacity shall be determined based on:
(1) Volume of
sludge added;
(2) Percent
solids and character;
(3) Temperature
to be maintained in the digesters;
(4) Mixing to
be obtained;
(5) Degree of
volatile solids reduction required. For
high rate digestion, the volatile solids loading shall not exceed 0.16 pounds
per cubic foot per day; and
(6) Allowance
for grit accumulation.
(c) If the digesters will serve as supernatant
separation tanks, the tank sidewater depth shall:
(1) Be a
minimum of 20 feet; and
(2) Allow for
the formation of supernatant liquor.
(d) Digester tanks shall be covered.
(e) Sludge mixing systems shall be capable of:
(1) Mixing
sludge to a uniform consistency; and
(2) Controlling
foam.
(f) Digestion tanks shall incorporate the
following features to facilitate emptying, cleaning, and maintenance:
(1) The tank
bottom shall slope to drain toward the withdrawal pipe at a slope of not less
than 3 inches per foot unless mechanical sludge collection is employed and then
slope of not less than one inch per foot;
(2) At least 2
access manholes having 36-inch diameters and one gas dome shall be provided in
the top of the tank with stairway access to the manholes;
(3) At least
one additional access manhole shall be provided and shall be large enough to
permit the mechanical removal of grit and sand;
(4)
Non-sparking tools, rubber-soled shoes, safety harness, gas detectors
for flammable and toxic gases, and gas masks of the hose or oxygen helmet type
shall be specified for use in the tanks; and
(5) Alarms
shall be installed to warn of:
a. Any drop of
the liquid level below minimum operating elevation; or
b. Low pressure
in the space above the liquid level.
(g) Digestion tanks shall incorporate the
following inlet and draw-off features:
(1) Multiple
sludge inlets and draw-offs ports and, where used, multiple recirculation
suction and discharge points, to facilitate flexible operation and effective
mixing of the digester contents shall be provided unless adequate mechanical
mixing facilities are provided within the digester;
(2) One inlet
shall discharge above the liquid level and be located at approximately the
center of the tank to assist in scum breakup;
(3) The inlet
discharge shall be isolated from the gas draw-off point of the cover; and
(4) Raw sludge
inlet discharge points shall be located so as to minimize short-circuiting.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.07 Anaerobic Sludge Digestion:
Piping and Appurtenances.
(a) Digester systems shall be equipped with
thermometers to monitor temperatures of the sludge, hot water feed, hot water
return,
and boiler water.
(b) All portions of the gas system, including the
space above the tank liquor, storage facilities, and piping, shall be designed such
that under normal operating conditions, including sludge withdrawal, the gas
shall be maintained under positive pressure.
(c) All occupied enclosed areas where gas leakage
might occur shall be mechanically ventilated in accordance with the NFPA as
incorporated by reference in the state fire code in Saf-C 6000 and NFPA 820, available as
noted in Appendix B.
(d) All gas metering, compressor, control, and
appurtenant equipment shall be located in a separate room with only an outside
entrance and equipped with a hazardous gas detection alarm system.
(e) Pressure and vacuum relief valves and flame
traps together with automatic safety shut-off valves shall be provided.
(f) The gas piping system shall be:
(1) Protected
from freezing;
(2) Sloped 1-2
percent to drain to condensation traps at all low points;
(3) Equipped
with either float-controlled or U-tube water seal type condensate traps;
(4) Corrosion
resistant; and
(5) Designed to
maintain digester gas velocities less than 12 feet per second.
(g) Gas burning boilers and engines shall be:
(1) Located in
ventilated rooms at ground level;
(2) Separated
from the digester gallery; and
(3) Equipped
with flame traps and pressure relief valves at a minimum.
(h) Cogeneration system design parameters shall
include:
(1) Volume of
gas produced by digesters;
(2) Digester
gas energy value in BTUs/cubic foot;
(3) Gas
composition;
(4) Gas storage
capability; and
(5) Gas
pretreatment requirements.
(i) Electrical
systems and equipment shall comply with the NEC requirements adopted by
reference in the state building code pursuant to RSA 155-A:1, IV, for the
installed locations.
(j) Digester pipe galleries shall be designed in
accordance with the NFPA as incorporated by reference in the state fire code in
Saf-C 6000 and NFPA 820, available as noted in Appendix B.
(k) Waste gas burners shall be accessible and
located:
(1) At least 25
feet away from any plant structure when placed at ground level; or
(2) On the roof
of a control building if they are:
a. Removed from
the tank; and
b. High enough
that flames will not be blown within 10 feet of the roof surface.
(l) A gas meter with by-pass shall be provided to
measure total gas production, per-tank gas production, and flared gas.
(m) Digestion tanks shall be insulated to
minimize heat loss.
(n) Sludge shall be heated by circulating the
sludge through external heaters and piping shall be designed to provide for the
preheating of feed sludge before introduction to the digesters. Provisions shall be made in the layout of the
piping and valving to facilitate cleaning of these lines.
(o) Where digestion gas is used for heating, an
auxiliary fuel shall be provided.
(p) For tanks where supernatant is withdrawn from
the digester, digester supernatant piping shall be:
(1) Not less
than 6 inches in diameter;
(2) Arranged so
that withdrawal can be made from 3 or more levels in the tank; and
(3) Equipped
with an unvalved emergency overflow designed to
prevent sludge discharge to the gas system that will convey digester overflow
to the WWTP headworks, the aeration process, or to another liquid sludge
storage facility and that has provisions for monitoring overflows and sounding
an alarm if and when an overflow occurs.
(q) Provision shall be made for sampling at each
supernatant draw-off level.
(r) High pressure backwash facilities shall be
provided for the piping system.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.08 Aerobic Sludge Digestion.
(a) Aerobic sludge digestion shall be
accomplished in a tank or tanks designed to provide effective air mixing,
reduction of the organic matter, and sludge concentration under controlled
conditions.
(b) Tank capacities shall be based on the
quantity of sludge produced and sludge characteristics including concentration
and aeration time.
(c) Volatile solids loading shall not exceed 300
pounds per 1,000 cubic feet of volume per day in the digestion units.
(d) A minimum of 15 days detention shall be
provided for waste activated sludge.
(e) A minimum of 20 days detention shall be
provided for primary sludge or any combination of waste activated sludge and
primary sludge.
(f) Duplicate tanks shall be provided unless an
alternative method of solids handling or storage has been provided for use when
a single digestion tank is not in service.
(g) Multiple tanks shall be designed to operate
either in series or in parallel.
(h) The minimum quantity of oxygen provided shall
be:
(1) Based on
2.1 pounds of oxygen per pound of volatile solids destroyed for open tank
systems; or
(2) Based on
1.5 pounds of oxygen per pound of volatile solids destroyed for thermophilic
systems.
(i) A minimum mixing
requirement of 30 cubic feet of air per minute per 1,000 cubic feet of tank
volume shall be provided.
(j) Facilities shall be provided for effective
scum and grease removal.
(k) Impact of supernatant on the wastewater
treatment process shall be included in the basis of design.
(l) Foam spray water piping and nozzles or other
mechanical foam control devices shall be provided.
(m) An unvalved
emergency overflow shall be provided that will convey digester overflow to the
WWTP headworks, the aeration process, or to another liquid sludge storage
facility and that has an alarm for high level conditions.
(n) The capacity of the blowers or air
compressors shall be based on the site pressure altitude, corrected to 100°F,
equivalent to 38°C, at 85% relative humidity.
By controlling the rate of air delivery, the drive motor shall not be
overloaded at full speed with site pressure altitude corrected to -22°F,
equivalent to ‑30°C.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 716.09 Gravity
Sludge Thickening.
(a) Duplicate gravity thickeners shall be
provided to allow the thickening process to continue without disruption with
one unit out of service.
(b) Mechanical picket arms shall be provided.
(c) The drive mechanism shall have:
(1) Sufficient
torque capacity to handle the maximum sludge concentration and blanket
thickness anticipated; and
(2) A high
torque alarm and overload device.
(d) An odor control system shall be
provided. Elutriation water may be used
for this purpose only in conjunction with additional odor control measures.
(e) Metallic components of gravity thickeners
shall be corrosion resistant.
(f) Gravity thickeners shall be designed on the
basis of the following:
(1) Primary
sludge solids loading of 20 to 30 pounds/day/square foot; and
(2) Combined
primary and waste activated sludge loading of 5 to 14 pounds/day/square foot.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 716.10 Mechanical
Sludge Thickening.
(a) Gravity belt, rotary drum, dissolved air
flotation, screw presses, and centrifuges shall be acceptable for mechanical
thickening of primary, secondary, and combined sludges.
(b) A means of chemically conditioning sludges
prior to mechanical thickening that meets the requirements of Env-Wq 716.12
shall be provided.
(c) Mechanical thickeners shall be capable of
processing the maximum weekly sludge production in 30 hours, unless the
equipment is designed to be operated unmanned.
(d) If any period of unmanned operation is
anticipated as a normal operating condition, then appropriate instrumentation
and fail safe monitoring and alarms shall be provided.
(e) Where duplicate units are not provided, a
contingency plan shall be submitted with the basis of design and sludge storage
facilities shall be provided that are adequate to store sludge for the period
of time anticipated for repairs to be made if the dewatering device is taken
out of service for repair.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.11 Sludge Pumps and Piping.
(a) Sludge pumping systems shall be designed with
adequate capacity to cover the full range of anticipated solids concentrations
and sludge production rates. Operating
pressures and head losses shall be calculated to account for the higher
friction factors associated with the type of sludge being pumped.
(b) Duplicate sludge feed pumps shall be
provided.
(c) Net positive suction head conditions
appropriate to pumping equipment flow and sludge characteristic variations
shall be provided.
(d) Sampling valves shall be installed at the
sludge pumps.
(e) Sludge withdrawal piping shall have a minimum
diameter of 6 inches. Sludge pump
discharge piping shall be at least 4 inches in diameter. Where withdrawal is by gravity, the available
head on the discharge pipe shall be at least 4 feet greater than the calculated
head loss. All sludge piping systems
shall be designed to provide a velocity of at least 2 feet per second.
(f) Provision shall be made for draining and
flushing discharge lines.
(g) Gravity piping shall be laid on uniform grade
and alignment. Slope on gravity
discharge piping shall be not less than 3 percent.
(h) Provision shall be made for draining and
flushing sludge processing lines.
(i) Piping installed
inside digestion tanks shall have the corrosion resistance and support
stability appropriate for a highly corrosive environment.
(j) For sludge pumping systems, alarms shall be
provided for:
(1) Pump
failure;
(2) Loss of
pressure; and
(3) High
pressure.
(k) Sludge pumps shall be equipped with high
pressure shutoff switches.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.12 Sludge Conditioning.
(a) Storage space shall be provided for
concentrated conditioning agents sufficient to maintain an inventory capable of
meeting the facility needs for maximum monthly production.
(b) Storage and handling facilities shall be
compatible with the material to be stored and shall comply with Env-Wq 708.06.
(c) Equipment shall be provided to allow for
proper and safe physical movement of the bulk material storage containers.
(d) Facilities shall be provided to allow the
wetting, mixing, and dilution of concentrated or dry conditioning agents and
for aging, storage, and mixing of dilute material in sufficient volume for at
least one day of sludge conditioning.
(e) Positive displacement pumps with a variable
feed rate shall be used to control the conditioning agent feed rate to the
point of use.
(f) Duplicate pumping systems shall be provided.
(g) The conditioning agent pumping system shall
be fitted with appropriate backpressure valves to assure delivery of the
correct volume of conditioning agent without being influenced by the volume in
the storage tank or the backpressure on the piping system.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 716.13 Mechanical
Sludge Dewatering.
(a) Mechanical devices acceptable to dewater
sludge shall include belt filter press, centrifuge, rotary press, pressure
filter press, and screw press.
(b) The proposed use of less common alternatives,
such as geotubes and rolloff
containers fitted with screens, shall require supporting documentation
demonstrating successful use in facilities similar to the proposed installation
under similar design criteria and conditions.
(c) Subject to (d), below, prior to selecting
mechanical dewatering equipment, pilot testing shall be used to establish
design criteria.
(d) For facilities in which sludge is not
available or is likely to change considerably in nature, successful performance
from multiple facilities handling similar sludges under similar conditions and
design criteria shall be documented and used to develop appropriate design
criteria.
(e) Mechanical dewatering units shall be capable
of handling the maximum weekly sludge production in 30 hours, unless the
equipment is designed for continuous operation.
(f) If any period of unmanned operation is
anticipated as a normal operating condition, then appropriate instrumentation
and fail safe monitoring and alarms shall be provided.
(g) Alarm systems shall be provided to notify the
operator(s) of conditions that could result in process equipment failure or
damage, a threat to operator safety, or a sludge spill or overflow condition.
(h) Belt presses and
conveyors shall be provided with emergency pull cords along the entire length
of the press that will:
(1) Stop the
press in an emergency; and
(2) Trigger an
audible alarm.
(i) Chemical feed
systems for sludge conditioning shall meet the requirements of Env-Wq 716.12.
(j) A hose station shall be provided to allow for
cleanup and wash-down of the dewatering area and equipment at the end of
dewatering operations.
(k) Ventilation of the dewatering area shall be
in accordance with the NFPA as incorporated by reference in the state fire code
in Saf-C 6000 and NFPA 820, available as noted in Appendix B, to minimize the buildup of
combustible gasses, odors, and humidity.
(l) Where duplicate sludge dewatering units are
not provided, a contingency plan shall be submitted with the basis of design,
and sludge storage facilities shall be provided that are adequate to store
sludge for the period of time anticipated for repairs to be made if the
dewatering device is taken out of service for repair.
(m) Sludge storage shall precede all mechanical
dewatering units and shall be provided by the use of holding tanks or
thickeners or chemical blending tanks, as required for the total dewatering
process operation.
(n) Dewatering sidestreams
shall be returned to the treatment process as far upstream as practicable prior
to the biological treatment unit.
(o) A means shall be provided for measuring the
quantity of sludge processed in both wet tons and dry tons.
(p) Dewatering process rooms shall be lighted,
heated, and ventilated, using energy efficient fixtures and equipment. Floors of process rooms shall be pitched 1/4
inch per foot to drain points and be slip proof.
(q) Sludge dewatering process equipment shall be
housed in processing rooms isolated from other portions of the WWTP.
(r) Electrical systems and equipment shall comply
with the NEC requirements adopted by reference in the state building code
pursuant to RSA 155-A:1, IV, for the installed location.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
716.14 Sludge Drying Beds.
(a) Sludge drying beds shall be sized based on
2.0 square feet per capita when the drying bed is the primary method of
dewatering and 1.0 square feet per capita when the drying bed is to be used as
a backup dewatering unit.
(b) Sludge drying beds shall include an
impervious membrane under the underdrain system.
(c) The lower course of gravel around the
underdrains shall be graded and a total of 12 inches in depth, extending 6
inches above the top of the underdrains.
A 3-inch layer of gravel 1/8-inch to 1/4-inch in size shall be placed
above the gravel bedding.
(d) The top layer of the bed shall consist of a
level-graded 9 to 12 inches of clean sand with an effective grain size of 0.3
to 0.6 mm or a comparably graded artificial media.
(e) Subnatant collected
from the underdrains shall be returned to the
treatment process prior to the biological treatment unit.
(f) Drying beds shall be covered to protect from
precipitation.
(g) Bed underdrains shall be ductile iron, HDPE,
PVC, or concrete pipe no less than 4 inches in diameter and spaced not more
than 10 feet between centers.
(h) Paved surface beds shall be prohibited.
(i) Bed walls shall
be watertight and extend 15 to 18 inches above the top layer or surrounding
topography, whichever is higher, and 6 inches below the invert of the
underdrain. Outer walls shall be curbed
to prevent soil from washing on to the beds.
(j) Not fewer than 2 beds shall be provided.
(k) Sludge drying beds shall be permitted in
accordance with Env-Or 700.
(l) Alternative dewatering methods or sludge
storage shall be provided during cold weather months when sludge drying beds
are not effective.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq 716.15 Additional
Required Features of Sludge Handling Processes.
(a) All essential components
of the solids handling processes shall be designed to provide duplicate units,
redundancy, or backup capabilities so that malfunction of any one component
will not result in interruption of the entire sludge handling process. Where duplicate units are not provided, a
contingency plan shall be submitted with the basis of design.
(b) Piping systems for solids handling shall
provide, for all reaches of the sludge piping:
(1) High
pressure flushing capability; and
(2) Sufficient
valving to allow for isolation of all unit processes.
(c) Clearance adequate to allow physical access
by WWTP staff shall be provided in and around solids handling equipment to
allow for:
(1) Inspection;
(2) Cleaning;
(3)
Lubrication;
(4) Removal and
repair of key components; and
(5) Routine
maintenance.
(d) Completely enclosed process units shall be
provided with inspection ports and 2 points of physical access through portals
or hatches.
(e) Control systems appropriate to the specific
solids handling process shall be provided to allow for manual and automatic
operation of the systems.
(f) Instrumentation and control devices shall be
provided to:
(1) Detect and
convey alarm conditions such as high liquid storage levels, equipment
misalignment or jamming, equipment failure, overheating, or over-torquing; and
(2) Shut down
solids handling processes for conditions that could cause damage to the system
or injury to the operator(s) or result in spills or overflows of liquids or
solids from the handling process.
(g) An operation and maintenance manual shall be
provided for the solids handling process that describes procedures for:
(1) Normal
operation;
(2) Adjustment
and calibration;
(3)
Troubleshooting;
(4) Maintenance
and repair; and
(5) Controls
for normal, bypass, and emergency conditions.
Source. (See Revision Note at chapter heading for
Env-Wq 700) #8590, eff 3-25-06; ss by #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 717
INNOVATIVE AND ALTERNATIVE TECHNOLOGIES
Env-Wq
717.01 Purpose and Applicability.
(a) The purpose of this part is to provide the
methodology and review process for the evaluation and approval of
innovative/alternative (I/A) waste treatment systems in compliance with RSA
485-A:4, IX.
(b) This part shall apply to all wastewater
treatment and conveyance technologies, including advanced treatment processes,
subject to review and approval under Env-Wq 701 through Env-Wq 716 and Env-Wq
718 through Env-Wq 719 and not expressly described therein.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.02 Operating Requirements.
(a) The owner shall operate and maintain I/A
wastewater treatment and conveyance systems in accordance with all applicable
laws and rules.
(b) The owner shall replace or modify an I/A
system if the technology fails to meet the intended purpose or discharge permit
limits or other requirements.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.03 Use of I/A Technology.
(a) No I/A wastewater treatment and conveyance
technologies shall be used in a full scale application at a municipal facility
until the technology has been evaluated and approved by the department.
(b) A pilot test shall be conducted pursuant to
Env-Wq 717.04 unless the proposed technology meets the criteria of Env-Wq
717.05(d).
(c) A proposed pilot test plan shall be submitted
to the department for review and approval at least 30 days prior to proceeding
with the pilot test.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.04 I/A Technology Pilot
Requirements.
(a) A pilot test plan shall include:
(1) A
description of proposed pilot unit equipment description and capacity, either
as:
a. Existing
treatment units parallel to the existing treatment process; or
b. A
stand-alone pilot;
(2) A proposed
schedule and duration, including:
a. A calendar
schedule with considerations for:
1. Seasonal
temperature variations relative to impact on process performance;
2. Seasonal
flow variations; and
3. Seasonal waste characterization variations; and
b. Pilot
duration and justification for proposed duration to account for seasonal
variations;
(3) Wastewater
feed characterization, including:
a. Historical
WWTP flow and waste characteristic data review;
b. Proposed
program for pilot wastewater characterization;
c. Wastewater
sampling and analysis plan; and
d. Pretreatment
requirements for the pilot equipment, if necessary;
(4) Proposed
pilot equipment configuration and set up, including:
a. Pilot feed
equipment and feed rate;
b. Pilot unit
description and proposed location on WWTP site;
c. Flow
measurement during pilot testing;
d. Pilot
control methodology;
e. Sample
collection and analysis plan during pilot testing; and
f. Proposed
modifications to the existing facility, if required;
(5) Pilot start
up plan, including:
a. Written
description of pilot start up plan;
b. Startup
monitoring and supervision; and
c. Proposed
process stabilization determination methodology; and
(6) Field
procedures and monitoring, including:
a. List of
parameters to be monitored;
b. Sampling
frequency and analysis for each parameter;
c. Type of
sampling, grab, or flow-proportional composite;
d. Sample
handling procedures used to assure quality assurance; and
e. Procedures
to address unusual events such as process upsets and equipment failures.
(b) A pilot test summary report shall be
completed and submitted for review, if needed pursuant to Env-Wq 717.05
and Env-Wq 717.06, and approval in accordance with Env-Wq
717.06(b), by the department within 60 days of pilot test conclusion
and prior to designing or constructing a full-scale system.
(c) The pilot test summary report shall include,
at a minimum:
(1) Executive
summary;
(2) Pilot
methodology;
(3) Sampling
and analysis methodologies;
(4) Test
procedures and methods;
(5) Complete
data summary;
(6) Data
analysis methodology;
(7) Analysis of
pilot performance; and
(8) Conclusions
and recommendations.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.05 I/A Technology Evaluation
Process.
(a) Anyone proposing an I/A technology that has
not been previously approved by the department shall submit a request to the
department for approval of the technology.
(b) The request submitted pursuant to (a), above,
shall include:
(1) A narrative
describing the proposed technology;
(2) A
discussion of applications or demonstration projects using the technology; and
(3) The
benefits expected from its use.
(c) If the proposed technology has not been
proven in full scale application but has been developed in documented research
and demonstration projects, a technology assessment report shall be prepared
and submitted to the department for review in accordance with Env-Wq
717.06. A pilot test shall be conducted
pursuant to the requirements of Env-Wq 717.04.
(d) If the proposed technology has been proven in
other applications at facilities with similar waste characteristics, and there
are multiple existing full scale applications in locations with climate
conditions similar to those in New Hampshire and design criteria and
operational data are available demonstrating the ability of the proposed
process to meet the proposed permit limits, then a basis of design using
available data in lieu of a pilot test shall be prepared and submitted in
accordance with Env-Wq 717.07.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.06 Technology Assessment Report
Submittal and Review.
(a) The technology assessment report specified in
Env-Wq 717.05(c) shall include:
(1) A written
description of the proposed I/A technology;
(2) A history
of where and when the technology was developed;
(3) Operational
reports, technical reports, and laboratory reports that resulted from research
or demonstration projects;
(4) A full
listing of all applications and tests of the technology;
(5) Records
regarding the length of time the technology has been operated and evaluated and
the climate conditions under which the testing was conducted;
(6)
Documentation of flow rates, volumes, and pollutant loadings during
demonstration projects and a discussion of how these loadings compare to full
scale operation;
(7) A
discussion of how the design criteria for the technology have been developed;
and
(8) A
discussion of the advantages of the proposed technology and risks associated
with adoption of the technology.
(b) The department shall evaluate the technology
assessment report to determine whether the proposed I/A technology meets the
following criteria:
(1) Whether the
proposed technology offers advantages over conventional technology in at least
one of the following areas:
a. Reduction of
life cycle costs;
b. More
efficient use of energy or resources;
c. Elimination
or reduction of discharge of pollutants; or
d. Recycling,
reclamation, or re-use of byproducts of the process;
(2) Whether the
technology appears promising based upon the results of research and
demonstration projects with benefits that outweigh the element of risk;
(3) Whether the
expected treatment results satisfy the requirements of the discharge permit;
(4) If
applicable, whether spare parts and servicing are available; and
(5) Whether the
I/A system is no more difficult to operate than a conventional WWTP and
provides at least the same level of protection to public health, the
environment, and the I/A system’s operators.
(c) The department shall respond to the
technology assessment report in writing within 60 days based upon its review of
the information submitted.
(d) If the department cannot determine whether
the proposal meets the criteria listed in (b), above, the department shall
identify the deficiencies and request the applicant to provide additional
information to address them.
(e) If the department determines that the
proposal meets the criteria listed in (b), above, and that conditions are not
necessary to protect public health, the environment, or operators, the
department shall approve the proposal.
(f) If the department determines that the
proposal meets the criteria listed in (b), above, but conditions are necessary
to protect public health, the environment, or operators, the department shall
approve the proposal with such conditions as are necessary.
(g) If the department determines that the
proposal does not meet the criteria listed in (b), above, or that no conditions
could be added that would be adequate to protect public health, the
environment, or operators, the department shall reject the proposal.
(h) If the department approves the proposal with
conditions or rejects the proposal, the written decision shall specifically
state the reason(s) for the decision.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.07 Basis of Design.
(a) Upon approval or conditional approval of the
technology assessment report, or pursuant to Env-Wq 717.05(d), the owner shall
submit a basis of design in accordance with Env-Wq 707 for the proposed
project.
(b) The department shall respond to the basis of
design within 60 days.
(c) The department shall accept the proposed
basis of design if the proposed basis of design appears to provide treatment
that will be adequate to satisfy the requirements of the discharge permit.
(d) Acceptance of the basis of design shall
constitute authorization to proceed with final design for the proposed I/A
technology project.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.08 Final Design. After acceptance of a basis of design, the
owner shall submit final plans and specifications for review and approval in
accordance with Env-Wq 703.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.09 Performance Assessment.
(a) During the first year of operation of an I/A
project, the owner shall submit 2 reports of performance to the department, the
first within 60 days after 6 months of operation and the second within 60 days
after 12 months of operation.
(b) The owner may request that the performance
assessment report schedule be extended in accordance with Env-Wq 717.10.
(c) The performance assessment report shall
include:
(1) Sampling
and analysis results for influent and effluent parameters;
(2) Calculated
loading rates during the performance period;
(3) An
assessment of benefits identified in the I/A technology assessment report;
(4) A
discussion of system performance process parameters determined to be critical
to proper operation and adjustments made during performance period; and
(5) An
assessment of the system’s ability to meet effluent criteria.
(d) The department shall review the performance
assessment report to determine whether to approve the system for continued
use. During the pendency of the review,
the owner may continue to use the I/A technology.
(e) The department shall approve the system for
continued use if the department determines that:
(1) The system
is capable of consistently meeting the limits of the discharge permit at
proposed loadings based upon performance during the assessment period; and
(2) No permit
violations resulting from the I/A technology occurred during the performance
assessment period for at least 3 consecutive months.
(f) If the department cannot accept the system,
the owner may prepare an action plan to obtain satisfactory performance and
submit the plan to the department. The
action plan shall clearly identify the cause(s) of unsatisfactory performance
and propose corrective measures.
(g) The department shall accept the action plan
if the proposed corrective measures appear adequate to remedy the cause(s) of
the unsatisfactory performance. If the
action plan is accepted by the department, the system shall undergo one
additional year of temporary operation and the owner shall submit 2 additional
performance reports to the department at 6-month intervals.
(h) If the action plan is not acceptable or if
the owner chooses to not submit an action plan, the owner shall remove the I/A
system or replace the system with a conventional system.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
717.10 Extension of Performance
Assessment Period.
(a) If the owner of an I/A system determines that
the performance assessment cannot be completed in one year, the owner shall
submit a written request for extension to the department.
(b) The request for extension shall contain the
following information:
(1) Facility
name and location;
(2) Date of I/A
technology approval;
(3) Type of I/A
technology system;
(4) Reason(s)
why the performance assessment cannot be completed in one year;
(5) Steps that
will be taken to complete the performance assessment; and
(6) Estimated
amount of additional time required to fully assess the system.
(c) The request shall be filed not less than one
month prior to the end of the one-year assessment period.
(d) The department shall respond to the request
in writing within 30 days of receipt of a request filed in accordance with (b)
and (c), above.
(e) The department shall grant the extension if
the department finds that:
(1) The
performance assessment cannot reasonably be completed in one year; and
(2) The steps
identified by the owner appear adequate to fully assess the I/A technology
system.
(f) If the department does not approve the
request for extension, the response provided pursuant to (d), above, shall
specify:
(1) The
reason(s) for the decision; and
(2) The
deadline for submittal of the second performance assessment report.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 718
OWNERSHIP OF WWTPs
Env-Wq
718.01 Purpose. The purpose of this part is to establish
conditions for issuance of discharge permits to privately-owned,
non-industrial WWTPs under the authority of RSA 485-A:13.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
718.02 Subsurface Disposal Options. No discharge permits for privately-owned,
non-industrial WWTPs discharging to surface water or groundwater shall be
issued unless all subsurface disposal options as regulated by RSA 485-A:29-44
and Env-Wq 1000 have been considered and rejected by the department based on
the criteria and procedures specified therein.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
718.03 Ownership Requirements. No discharge permits for WWTPs discharging to
surface water or groundwater shall be issued unless the WWTP is:
(a) Municipally owned and operated;
(b) Municipally owned with a private contract for
operations and maintenance;
(c) Privately-owned where connection to a
municipal system is not possible, provided that:
(1) The
municipality in which the WWTP is proposed agrees by affirmative vote of the
local legislative body to be the holder or co-holder of any discharge permits
issued; and
(2) The
documentation requirements of Env-Wq 718.05 are met; or
(d) Privately-owned where:
(1) Municipal
ownership is not possible, connection to municipal system is not possible, and
the municipality in which the facility is located refuses to hold or co-hold
the discharge permit, as shown by a negative vote of the local legislative
body; and
(2) The
documentation requirements of Env-Wq 718.05 are met.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
718.04 Capacity.
(a) Private ownership as allowed under Env-Wq
718.03(c) and (d) shall be limited to WWTPs with design flow capacities of
50,000 gpd or greater. The department
shall not approve a WWTP designed with a capacity of 50,000 gpd or greater for
the sole purpose of meeting this requirement when such capacity is not
justified by anticipated demand.
(b) WWTPs constructed to replace or rehabilitate
an existing failed subsurface disposal system shall not be subject to the size
restriction of (a) above, but shall otherwise meet the requirements of Env-Wq
718.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
718.05 Technical Documentation
Requirements. An applicant for a
discharge permit for a privately-owned WWTP as specified in Env-Wq 718.03(c) or
(d) shall submit to the department:
(a) The following technical documentation:
(1) Engineering
and water quality studies as required to demonstrate that the proposed facility
is consistent with statewide, area-wide, or regional water quality planning
pursuant to sections 205(j)(1), 205(j)(5), or 208 of the federal Water
Pollution Control Act of 1972, as amended;
(2) Engineering
and water quality studies to demonstrate that the discharge is consistent with
the water quality goals as provided in RSA 485-A:8 and Env-Wq 1700 relative to
water quality standards;
(3) Evidence in
the form of certification from the municipality that the system proposed has
the concurrence of the local governing body and local land use boards as
defined in RSA 672;
(4) Technical
design drawings and specifications in accordance with this chapter;
(5)
Certification by a New Hampshire-licensed professional engineer that the
facilities have been built in accordance with the approved plans and
specifications, which certification shall be submitted within 60 days following
substantial completion of construction of the WWTP; and
(6) Evidence in
the form of a written agreement that the WWTP will be operated by an operator
certified under Env-Wq 900; and
(b) Within 60 days following substantial
completion of construction of the WWTP or pump station(s), operation and
maintenance manuals to provide information and guidance for day-to-day
operation of the WWTP and pump stations, as applicable, that contain the
following information:
(1) Information
on process design assumptions;
(2) Unit
process information that includes control measures and monitoring procedures
for the various processes;
(3) Start-up
procedures for each unit operation and piece of equipment;
(4) Maintenance
management systems;
(5) Laboratory
test procedures;
(6) Safety
procedures;
(7)
Organizational structure and administrative procedures;
(8)
Troubleshooting procedures;
(9) Emergency
operation plan;
(10) Staffing
requirements;
(11) Process
and instrumentation diagram; and
(12) Checklists
for systems and components for operator’s use in developing a maintenance
program for pump stations and WWTPs.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
718.06 Financial Documentation
Requirements. An applicant for a
discharge permit for a privately-owned WWTP as specified in Env-Wq 718.03(c) or
(d) shall submit the following financial documentation:
(a) A system for assessing the users of the WWTP,
which system shall:
(1) Assess
users on a pro rata basis;
(2) Generate
sufficient funds to be used to cover all expenses and charges related to the
operation, maintenance, routine repair and replacement, and financing of the
WWTP;
(3) Include
provisions for calculating the assessments based on the total costs enumerated
in (2) above;
(4) Include
provisions for notifying users of the amounts due, collecting the amounts due
on a periodic basis, and rebating excess collections or applying excess
collections to the next billing period; and
(5) At the
owner’s discretion, include provisions for terminating service or assessing and
collecting penalties for non-payment;
(b) Evidence of a capital reserve account, which
account shall:
(1) Be
sufficient to cover the cost of replacement of the WWTP within 20 years;
(2) Serve as a
source of funds for emergency cleanup and containment and major repairs or
replacement of system components;
(3) Be
established prior to initiation of operation of the WWTP;
(4) Identify
the situations in which the account may be accessed;
(5) Restrict
account payments for repair and replacement costs to those in excess of $2,000;
(6) Be
sheltered from liability or bankruptcy claims, attachments, or other such
liens;
(7) Provide for
management of the account and bonding of the account managers;
(8) Authorize
access to the account by the department for use in remedying an emergency
situation in cases where the managers of the account refuse to remedy the
emergency situation; and
(9) Provide for
funding the account; and
(c) Ownership documentation, comprising:
(1) Documents
that evidence the owner’s legal authority to construct and provide continuous
operations and maintenance of the facilities which include one of the
following:
a. The articles
of incorporation for a private corporation;
b. The
partnership agreement for a partnership; or
c. The
condominium instruments for a condominium association;
(2) For
issuance of a permit pursuant to Env-Wq 718.03(c), a formal written and
executed agreement between the owner and the municipality that the municipality
has agreed to be the holder or co-holder of the discharge permit; and
(3) For
issuance of a permit pursuant to Env-Wq 718.03(d), a docket number from the New
Hampshire public utilities commission showing that the facility owner is or
will be a company subject to, and in full compliance with, the rules of the New
Hampshire public utilities commission.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
PART Env-Wq 719
WAIVERS
Env-Wq
719.01 Purpose. The purpose of the rules in this part is to
establish the procedures and criteria under which the owner of proposed
sewerage or WWTP may seek waiver relief from specific rules contained in Env-Wq
700 when strict compliance with all rules is not in the best interests of
public health, the environment, and WWTP operators.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
719.02 Waiver Requests.
(a) The WWTP owner, or a duly-authorized
representative of the owner, shall request a waiver by submitting the following
information in writing to the department:
(1) The name,
mailing address, and daytime telephone number of the WWTP owner and, if
available, a fax number and email address;
(2) The name,
mailing address, and daytime telephone number and, if available, the fax number
and email address of the person requesting the waiver, if other than the owner;
(3) A reference
to the specific rule for which a waiver is requested;
(4) An
explanation of why the waiver is necessary, including an explanation of the
operational and economic consequences of complying with the rule as written;
(5) Whether the
waiver is needed for a specific period of time and, if so, the length of time
the waiver is needed;
(6) If an
alternative method, procedure, or design is proposed in lieu of the requirement
for which the waiver is requested, supporting data and calculations to show the
efficacy of the alternative in protecting public health, the environment, and
WWTP operators;
(7) If the
request is not filed by the governing body of the municipality, written
concurrence from such governing body; and
(8) An
explanation of how granting the request would be consistent with the criteria
specified in Env-Wq 719.03(a).
(b) The requestor and the owner, if other than
the requestor, shall sign and date the waiver request.
(c) The signature(s) shall constitute
certification that:
(1) The
information provided is true, complete, and not misleading to the knowledge and
belief of the signer; and
(2) The signer
understands that the submission of false, incomplete, or misleading information
is grounds for denying the waiver request or revoking
any waiver that is granted based on the information.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Env-Wq
719.03 Decisions on Waiver Requests.
(a) The department shall grant a waiver if it
determines that:
(1) The
requirement that is the subject of the request is not established in state or
federal statute or federal regulations or the state or federal statute or
federal regulation that establishes the requirement expressly provides that it
can be waived; and
(2) Granting a
waiver will not result in a lower level of protection of public health, the
environment, and WWTP operators as complying with the requirement as written.
(b) The department shall include such conditions
in the waiver as are necessary to ensure the criteria of (a), above, are met.
(c) If the waiver is needed for a finite period
of time, the department shall specify the expiration date of the waiver.
(d) The department shall notify the owner of its
decision on the waiver request in writing.
If the request is denied, the decision shall specify the reason(s) for
the denial.
Source. #10693, eff 10-15-14; ss by #14258, eff
7-1-25, EXPIRES: 7-1-35
Appendix A: Statutes Implemented
|
Rule
Section(s) |
State
Statute(s) Implemented |
|
Env-Wq 701 |
RSA 485-A:4, VI; RSA 485-A:4, IX |
|
Env-Wq 702 |
RSA 485-A:4, VI; RSA 485-A:4, IX |
|
Env-Wq 703 |
RSA 485-A:4, VI; RSA 485-A:4, IX |
|
Env-Wq 704 |
RSA 485-A:4, IX |
|
Env-Wq 705 |
RSA 485-A:4, IX |
|
Env-Wq 706 |
RSA 485-A:4, IX |
|
Env-Wq 707 |
RSA 485-A:4, IX |
|
Env-Wq 708 |
RSA 485-A:4, IX |
|
Env-Wq 709 |
RSA 485-A:4, IX |
|
Env-Wq 710 |
RSA 485-A:4, IX |
|
Env-Wq 711 |
RSA 485-A:4, IX |
|
Env-Wq 712 |
RSA 485-A:4, IX |
|
Env-Wq 713 |
RSA 485-A:4, IX |
|
Env-Wq 714 |
RSA 485-A:4, IX |
|
Env-Wq 715 |
RSA 485-A:4, IX |
|
Env-Wq 716 |
RSA 485-A:4, IX |
|
Env-Wq 717 |
RSA 485-A:4, IX |
|
Env-Wq 718 |
RSA 485-A:13, I (a) |
|
Env-Wq 719 |
RSA 541-A:22, IV |
Appendix B: Incorporation by
Reference
|
Title |
Obtain at: |
|
|
Env-Wq 704.03(b)(1) & (2) |
“Wastewater Engineering: Treatment and Resource
Recovery”, Metcalf & Eddy /AECOM, 5th Edition, 2014 |
McGraw Hill Education 2 Penn Plaza Online: https://www.mheducation.com/highered/product/M9780073401188.html Cost: $280.16 |
|
Env-Wq 704.03(d) Env-Wq 708.07(l)(1) & (2) Env-Wq 711.03(b)(3) |
TR-16, “Guides for the Design of
Wastewater Treatment Works” (revised 2016) |
New England Interstate Water
Pollution Control Commission Wannalancit Mills 650 Suffolk Street, Suite 410 Lowell, MA 01854 https://neiwpcc.org/news-publications/technical-guides/ Cost: $95 Hardcopy;
$25 USB |
|
Env-Wq 704.05(a)(1) |
AWWA C151/A21.51-23, “Ductile-Iron
Pipe, Centrifugally Cast” |
American Water Works Association Online: https://store.awwa.org/AWWA-C151-A21.51-23-Ductile-Iron-Pipe-Centrifugally-Cast Cost: $142 ($99 for members) |
|
Rule |
Title |
Obtain at: |
|
Env-Wq 704.05(a)(2) |
AWWA C150/A21.50-21 (R23),
“Thickness Design of Ductile-Iron Pipe” |
American Water Works Association Online: https://store.awwa.org/AWWA-C150-A21.50-21R23-Thickness-Design-of-Ductile-Iron-Pipe Cost: $142 ($99 for members) |
|
Env-Wq 704.05(a)(2) |
ASTM A536-24, "Standard Specification for
Ductile Iron Castings" |
ASTM International Online: https://store.astm.org/a0536-24.html Cost: $69 for PDF |
|
Env-Wq Table 704-2 |
ASTM D3034-24, "Standard Specification for Type
PSM Poly(Vinyl Chloride) (PVC) Sewer Pipe and Fittings" |
ASTM International Online: https://store.astm.org/d3034-24.html Cost: $91 for PDF |
|
Env-Wq Table 704-2 |
ASTM F794-21, "Standard Specification for
Poly(Vinyl Chloride) (PVC) Profile Gravity Sewer Pipe and Fittings Based on
Controlled Inside Diameter" |
ASTM International Online: https://store.astm.org/f0794-21.html Cost: $69 for PDF |
|
Env-Wq Table 704-2 |
ASTM F1760-16R20, "Standard Specification for
Coextruded Poly(Vinyl Chloride) (PVC) Non-Pressure Plastic Pipe Having
Reprocessed-Recycled Content" |
ASTM International Online: https://store.astm.org/f1760-16r20.html Cost: $69 for PDF |
|
Env-Wq 704.05(d) |
ASTM D2412-21, "Standard Test Method for
Determination of External Loading Characteristics of Plastic Pipe by
Parallel-Plate Loading" |
ASTM International Online: https://store.astm.org/d2412-21.html Cost: $69 for PDF |
|
Env-Wq 704.05(e) |
ASTM D3212-21, "Standard Specification for
Joints for Drain and Sewer Plastic Pipes Using Flexible Elastomeric
Seals" |
ASTM International Online: https://store.astm.org/d3212-21.html Cost: $61 for PDF |
|
Env-Wq 704.05(f) |
AWWA C302-22, "Reinforced Concrete Pressure
Pipe, Noncylinder Type" |
American Water Works Association Online: https://store.awwa.org/AWWA-C302-22-Reinforced-Concrete-Pressure-Pipe-Noncylinder-Type Cost: $142 ($99 member price) |
|
Rule |
Title |
Obtain at: |
|
Env-Wq 704.05(g) Env-Wq 704.05(h) |
AWWA C301-14(R19), "Prestressed Concrete
Pressure Pipe, Steel-Cylinder Type" |
American Water Works Association Online: https://store.awwa.org/AWWA-C301-14R19-Prestressed-Concrete-Pressure-Pipe-Steel-Cylinder-Type-PDF Cost: $142 ($99 member price) |
|
Env-Wq 704.06(b)(1) |
ASTM F1417-11a (2024), "Standard Practice for
Installation Acceptance of Plastic Non-Pressure Sewer Lines Using
Low-Pressure Air" |
ASTM International Online: https://store.astm.org/f1417-11ar24.html Cost: $83 for PDF |
|
Env-Wq 704.06(b)(2) |
Uni-B-6, "Recommended
Practice for Low-Pressure Air Testing of Installed Sewer Pipe" (1998) |
Uni-Bell PVC Pipe Association Online: https://www.uni-bell.org/Portals/0/ResourceFile/uni-b-6-98.pdf Cost: Free |
|
Env-Wq 704.08(c) |
ASTM D2241-24, "Standard Specification for
Poly(Vinyl Chloride) (PVC) Pressure-Rated Pipe (SDR Series)" |
ASTM International Online: https://store.astm.org/d2241-24.html Cost: $69 for PDF |
|
Env-Wq 704.08(c) |
ASTM D1785-21a, "Standard Specification for
Poly(Vinyl Chloride) (PVC) Plastic Pipe, Schedules 40, 80, and 120" |
ASTM Internatinonal Online: https://store.astm.org/d1785-21a.html Cost: $76 for PDF |
|
Env-Wq 704.08(d) |
ASTM D3035-22, "Standard Specification for
Polyethylene (PE) Plastic Pipe (DR-PR) Based on Controlled Outside
Diameter" |
ASTM International Online: https://store.astm.org/d3035-22.html Cost: $69 for PDF |
|
Env-Wq 704.08(d) |
ASTM F714-24, " Standard Specification for
Polyethylene (PE) Plastic Pipe (DR-PR) Based on Outside Diameter" |
ASTM International Online: https://store.astm.org/f0714-24.html Cost: $91 for PDF |
|
Env-Wq 704.09 |
AWWA C600-23, “Installation of Ductile-Iron Water
Mains and Their Appurtenances” |
American Water Works Association Online: http://www.awwa.org/publications/standards.aspx Cost: $142 ($99 for members) |
|
Rule |
Title |
Obtain at: |
|
Env-Wq 704.11(a) Env-Wq 704.12(r) Env-Wq 704.13(c)(5) |
ASTM C33/C33M-24a, "Standard Specification for
Concrete Aggregates" |
ASTM International Online: https://www.astm.org/standards-and-solutions/standards-publications Cost: $69 for PDF |
|
Env-Wq 704.11(k) Env-Wq 704.13(a)(1), (2) Env-Wq 704.13(c)(6) |
New Hampshire Department of
Transportation, “Standard
Specifications for Road and Bridge Construction” (2016) |
Available for no cost at: https://www.dot.nh.gov/sites/g/files/ehbemt811/files/inline-documents/2016-nhdot-spec-book-web.pdf |
|
Env-Wq 704.13(a)(3) Env-Wq 704.14(d) |
ASTM C478/C478M-22, "Standard Specification for
Circular Precast Reinforced Concrete Manhole Sections" |
ASTM International Online: https://store.astm.org/c0478_c0478m-22.html Cost: $69 for PDF |
|
Env-Wq 704.13(a)(8) |
ASTM A48/A48M-22, "Standard Specification for
Gray Iron Castings" |
ASTM International Online: https://store.astm.org/a0048_a0048m-22.html Cost: $69 for PDF |
|
Env-Wq 704.13(a)(9) Env-Wq 704.13(b)(1) |
ASTM C32-23, "Standard Specification for Sewer
and Manhole Brick (Made From Clay or Shale)" |
ASTM International Online: https://store.astm.org/c0032-23.html Cost: $61 for PDF |
|
Env-Wq 704.13(c)(3) |
ASTM C150/C150M-24, "Standard Specification for
Portland Cement" |
ASTM International Online: https://store.astm.org/c0150_c0150m-24.html Cost: $69 for PDF |
|
Env-Wq 704.13(c)(4) |
ASTM C207-24, "Standard Specification for
Hydrated Lime for Masonry Purposes" |
ASTM International Online:
https://store.astm.org/c0207-24.html Cost: $61 for PDF |
|
Env-Wq 704.17(a) |
ASTM C1244/C1244M-20, "Standard Test Method for
Concrete Sewer Manholes by the Negative Air Pressure (Vacuum) Test Prior to
Backfill" |
ASTM International Online: https://store.astm.org/c1244_c1244m-20.html Cost: $61 for PDF |
|
Rule |
Title |
Obtain at: |
|
Env-Wq 705.07(c)(2) Env-Wq 705.07(d) Env-Wq 705.08(a) Env-Wq 705.09(b)(10) Env-Wq 705.11(b) Env-Wq 708.20(d) Env-Wq 708.20(f) Env-Wq 708.20(h) Env-Wq 708.22(c) Env-Wq 716.07(c) Env-Wq 716.07(j) Env-Wq 716.13(k) |
NFPA 820, “Standard for Fire Protection in
Wastewater Treatment and Collection Facilities” (2024) |
National Fire Protection Association Online: https://www.nfpa.org/product/nfpa-820-standard/p0820code Cost: $149 ($141.30 for members) |
|
Env-Wq 706.03(f) |
“New Hampshire Coastal Flood Risk Summary – Part I:
Science and Part II: Guidance for Using Scientific Projections",
prepared for the New Hampshire Coastal Flood Risk Science and Technical
Advisory Panel |
NH
Department of Environmental Services office; or University
of New Hampshire https://scholars.unh.edu/ersc/210 and https://scholars.unh.edu/ersc/211/ |
|
Env-Wq 708.21(d) |
ANSI/ISEA Z358.1-2014 (R2020), “American National
Standard for Emergency Eyewash and Shower Equipment” |
American National
Standards Institute https://webstore.ansi.org/standards/isea/ansiiseaz3582014 Cost: $65 for PDF |
Appendix C: Statutory References
RSA 21:47
When used to refer to a municipality, and in the
absence of applicable chapter or subdivision definitions, the term
"legislative body" shall mean a town meeting, school district
meeting, village district meeting, city or town council, mayor and council,
mayor and board of aldermen, or, when used to refer to unincorporated towns or
unorganized places, or both, the county convention.
RSA 485-A:2
VI. “Industrial
Waste” means any liquid, gaseous or solid waste substance resulting from any
process of industry, manufacturing trade or business or from development of any
natural resources.
IX. “Person”
means any municipality, governmental subdivision, public or private
corporation, individual, partnership, or other entity.
X. “Sewage”
means the water-carried waste products from buildings, public or private,
together with such groundwater infiltration and surface water as may be
present.
XVI-a.
“Wastewater treatment plant (WWTP)” means the treatment facility or
group of treatment devices which treats domestic or combined domestic and
industrial wastewater through alteration, alone or in combination, of the
physical, chemical, or bacteriological quality of the wastewater and which
dewaters and handles sludge removed from the wastewater.
RSA 485-A:4
IX-a. Any person submitting plans and specifications
to the department, as provided for in this section, for the construction of
sewerage systems shall pay to the department a fee of $30 for each 300 gallon
per day unit of flow for the first 10,000 gallons per day of total flow for
which such systems are designed and $15 for each 300 gallon per day unit of
flow in excess of such amount. A fee of $200 per plan sheet shall be paid for
review of pump stations, force mains, interceptors, and wastewater treatment
facilities which are submitted independently of a sewer collection system. This
fee shall not apply to municipalities.