Document MJYmKoB1gzm1YRmjgjaNrY167
UNITED STATESUNITED STATES ENVIRONMENTAL PROTECTION AGENCY
* *REGION 1
ENVIRONMENTAL
AGENCY5 POST OFFICEB OSSTQOUN,A RMAE ,0 21S0U9-I3T9E12
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PROTECTION
Drafted Date:August 30, 2022
Finalized Date:Dated as shown on electronic signature
Subj:Inspection Report
Clean Water Act
From:Elizabeth Kudarauskas, Inspector
Douglas Koopman, Inspector
Damian Bednarz, Inspector
Thru:Elizabeth Kudarauskas
To:File
ELIZABETHDigitally signed by ELIZABETH
KUDARAUSKAS
KUDARAUSKASDate: 2022.09.20 15:05:45 -04'00 '
I. Facility Information
A. Facility Name:East Fitchburg Wastewater Treatment Facility (WWTF)
B. Facility Location: 24 Lanides Lane, Fitchburg, MA 01420
C. Facility Contacts: Mark McNamara - Superintendent, Wastewater Plant
Operations
Ken Letorneau - - Wastewater Plant Maintenance
Nick Erickson - Commission Public Works
Ken Dupant - Sewer System Manager
Matt Hotan - Weston & Sampson
D. NPDES ID No (s): MA0100986
II. Background Information
A. Date(s) of inspection: July 20, 2022
B. Weather Conditions: Clear and sunny, approximately 90 F
C. US EPA Representative(s): Elizabeth Kudarauskas, Douglas Koopman, Damian
Bednarz
D. State / Local Representative(s): Xiaoning Chen, MassDEP
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E. Federally Enforceable Requirements Covered During the Inspection:
NPDES Permit Number MA0100986, City of Fitchburg Wastewater
Treatment Facilities Commission effective September 1, 2010
Consent Decree United States and Massachusetts v. City of Fitchburg,
Filed 10/2/2012
F. Previous Enforcement Actions:
Consent Decree United States and Massachusetts v. City of Fitchburg,
Filed 10/2/2012
III. Type and Purpose of Inspection
U.S. Environmental Protection Agency (" EPA ") inspectors, Elizabeth Kudarauskas,
Douglas Koopman, and Damian Bednarz (" inspection team ") conducted an announced
inspection of the City of Fitchburg (" City ") Wastewater Treatment Facilities under
EPA's National Pollutant Discharge Elimination System (" NPDES ") individual discharge
permitting program. The inspection included the Fitchburg East Wastewater Treatment
Facility (the " Facility " or the " Site ") as well as a discussion of the City's collection
system and Combined Sewer Overflows (" CSOs ").
IV. Facility Description
The City provides sewage collection through a system of combined and separate sanitary
sewers. According to an inspection report drafted in February of 2019, the City's
wastewater collection system consists of about 133 miles of separate sanitary lines and 9
miles of combined sewer lines. Waste is treated at the Facility and effluent is discharged
into the North Nashua River. The City is permitted to discharge from 17 CSOs into the
following receiving waters: North Nashua River, Sand Brook, Birch Brook, Baker Brook,
and unnamed tributaries.
The Facility staff includes 21 staff members, including operations, maintenance, and
management positions. According to City personnel, at the time of the inspection, the
Facility was providing preliminary, primary, and secondary treatment for an average of
5.7 MGD, while the Facility design flow is 12.4 MGD. During wet weather, the Facility
can treat up to 25 MGD before bypassing secondary treatment. Flows are composed of
66% residential sources, with the remainder consisting of commercial and industrial
sources including 35,000 gallons per day of septage and 200,000 gallons per day from
Greif Paper Co. The Facility serves Fitchburg residents and businesses as well as the
neighboring communities of Lunenburg (allotted 161,000 gallons per day) and
Westminster (allotted 300,000 gallons per day).
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V. Inspection
Inspector Kudarauskas announced the inspection by email to Mr. McNamara on June 24,
2022.
The inspection team along with Xiaoning Chen from the Massachusetts Department of
Environmental Protection (" MassDEP ") arrived at the Facility at approximately 9:00
AM.
A. Opening Conference
The inspection team was granted access to the facility and began the opening conference
in the employee break room area. The inspection team presented credentials and began
with introductions.
Facility operators expressed that current flow average is 5.7 MGD, which is unusually
low. In the year prior the Facility had averaged 10 MGD. The Facility had not had a
bypass for a few months. Wet events have been relatively infrequent, and Facility
operations believes this might correlate to the lower flows.
Facility personnel described an upset of the plant that occurred in May 2022 and is still
impacting Facility operations. For one hour on Saturday of Memorial Day weekend, the
Facility saw a spike in the influent pH of 10.5. At the time of the inspection the Facility
was continuing to investigate possible sources of the pH spike. The inspectors discussed
possible sources, including industrial users. The Facility pH monitor is continuous and
has an alarm, but facility personnel were not sure if the pH alarm was also audible.
The Facility's supervisory control and data acquisition (" SCADA ") system stores and
monitors data from the treatment process and flow from the collection system pump
stations.
The Facility accepts up to 35,000 gallons of septage per day. Previously the Facility
accepted up to 100,000 gallons or more per day, but this led to too many problems with
facility operations. The Facility further restricts septage by not accepting it within two
hours of an anticipated wet weather event. This is maintained via controls that
automatically lock hook ups and valves during wet weather events. No septage enters the
headworks during bypass conditions. In 2020, the Facility completed its Comprehensive
Enhanced Phosphorus Treatment (" CEPT ") upgrade. Additionally, the secondary
treatment system was upgraded to include replacement of pumps and blowers and
recoating of pipes. Three emergency diesel generators were installed on Site, which are
run for maintenance every two weeks. The facility plans to upgrade their lab and replace
their gravity thickeners, which were initially installed in 1975. Additional upgrades
include adding a polymer to the sludge press, which increased solid waste concentration
from 1% to 5-7%.
In 2009, the City closed its Western WWTF and rerouted its flow to the Facility. Last
year, the City completed a separation project that resulted in separating a mile of
combined sewer lines. Facility staff stated that prior to the separation work that has
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already been completed, large storms would result in elevated flows at the Facility that
would last for days. Now that some separation work has been completed storm related
flow surges drop back down much faster. In addition, Facility staff noted that they have
seen a significant reduction of grit at the Facility since the separation work has started.
This year the City approved a downtown CSO project. This project is estimated to cost
$ 30 million to separate 5 miles of combined sewers. The project will be completed in
phases, with $ 10 million going towards Phase I, about a third of the work, and will start
in 2023. Phase II will address a larger area of the City and will start construction in 2024.
Phase II is expected to cover two construction seasons and will cost $ 20 million. These
projects will close another four CSOs and will include removal of inflow and infiltration
to bring a huge benefit to the Facility. At the time of the inspection the City was in the
process of conducting a sewer rate study because rates were expected to increase to fund
the separation projects. The City expects a fully separated stormwater system by 2030.
The City of Fitchburg also has combined manholes within the collection system.
Combined manholes are being separated as part of these projects. On average the City
has been separating about 25-30 combined manholes per year. Facility staff estimate an
average cost of $ 20,000 to $ 30,000 to separate each manhole, with extremes on both
sides of the estimate.
The City maintains a list of problem areas within the collection system. The City uses a
GIP map to track areas that are problematic due to roots, fats, oils and grease, or other
reasons. The local Board of Health and the Sewer Department work together on this
issue, and the Board of Health had enforcement authority if needed.
B. Facility Tour
At approximately 11am facility personnel, along with Mr. Hotan, led the inspection team
on a tour of the facility. The inspection team first saw the area where trucks connect to
the Facility to discharge septage via exterior hook up piping (image 191). A drain in the
septage area leads to the Facility headworks.
The inspectors then visited the headworks building where they observed two mechanical
bar racks and two aerated grit tanks (image 194). Settled solids are scooped out (image
196) of the grit tanks and put into dumpsters for disposal. Approximately 4-5 dumpsters
of grit are removed from each tank per year. Influent is sampled (image 197) and stored
in a refrigerator after the influent passes through both aerated grit and mechanical bar
screens (image 199-200). The bar racks are operated by a float or on a timer under
normal flow conditions. Rags from the bar racks are cleared and put in a dumpster. Odors
from the headworks building are managed with an odor control system.
The Facility previously had a multi - hearth sludge incinerator. The equipment is still on
site, however, it is no longer used. The old ash collection area is now used to collect
sludge in dumpsters. According to facility personnel, the Facility currently fills two
dumpsters per day with sludge.
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Inside the CEPT building the inspectors observed several large chemical storage tanks.
The tanks contained Sodium Hydroxide, Sodium Hypochlorite, Magnesium Chloride,
Polymers, and Ferric Chloride that are used for both 1st and 2nd stage aeration and
clarification (images 202-205). Mr. McNamara stated that most of the large tanks in the
CEPT building have a capacity of 7,200 gallons, except for the sodium hypochlorite tank,
which has a capacity of 5,800 gallons. Facility personnel also stated that the CEPT
building has sumps in the floor that would direct flow to the head of the plant if needed.
At the time of the inspection, the pumps were set in manual mode.
Outside the CEPT building the inspectors observed tanks that are used in the sludge
process. Two sludge gravity thickener tanks, two thickened waste activated sludge
(TWAS) holding tanks (image 206). and three primary settling tanks are in this area. All
of these tanks are covered and connected to the Facility odor control system.
Sludge is collected throughout the wastewater treatment process and directed first to the
three primary settling tanks. From the primary settling tanks sludge passes through two
gravity belt thickeners to increase the solids content. From the gravity belt thickeners the
sludge is held in the TWAS tanks, before it is sent back into the wastewater treatment
process. Fournier presses, located in a different area of the Facility, pull sludge off the
gravity belt thickeners to be further dewatered and sent to the Fitchburg - Westminster
landfill. Facility personnel stated that the sludge tanks are emptied, cleaned, and grit
removed once or twice per year for maintenance.
The inspectors then observed the process control sample station and the Facility's flow
meter. The first flow meter at the facility is located just before the aeration tanks (images
209-210). This flow meter, a Parshall flume, is used as the Facility's influent flow
measurement. At the time of the inspection, the plant was operating at about 5.75 mgd.
This flow measurement is used to control a bypass of secondary treatment, which is
necessary at flows greater than 25 mgd. Facility personnel stated that the Facility had
installed a new bypass flow meter that would comply with the new state CSO notification
requirements.
As facility personnel explained, after the flow meter, the flow splits and 60% of the
Facility flow goes into the second stage aeration tanks and 40% goes into the first stage
aeration tanks for further treatment (image 211-212). The first and second stage processes
are the same, but the second stage has slightly more capacity.
As part of the recent secondary treatment upgrades, the Facility added selector zones to
the beginning of each aeration chamber to increase nutrient removal. At the end of each
aeration chamber, the water flows over a weir where a polymer and then ferric chloride
are added for phosphorus removal.
At the time of the inspection the first stage # 2 clarifier was going offline and the # 1
clarifier was coming online. The facility stated that they need to clean the clarifiers once
or twice per week to minimize algae buildup.
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The inspectors first saw the pump galley for the first stage process, as well as the
centrifugal blowers used in the first stage aeration. The second stage blowers had been
replaced and are AERZEN Bowers. Facility personnel stated that the new blowers are
automatic and will ramp up based on the DO readings in the aeration tanks.
After the aeration process, the flow from the first and second stage combine in a mixing
box where sodium hypochloride is added for disinfection in the chlorine contact chamber.
The chlorine contact chamber (image 221) is the final treatment stage before
dechlorination and the effluent outfall. In the event of a bypass of secondary treatment,
the excess flow will pass through chlorination and dechlorination before discharge. At the
time of the inspection, the inspection team observed a scum on top of the chlorine contact
chamber (image 222 and 224). Facility personnel stated that the scum was the result of
the ongoing impacts of the Facility upset. The scum is cleaned from this area once per
week.
The Facility effluent flow measurement is taken at the weir on each side of the chlorine
contact chamber. These flow measurements are combined in the Facility SCADA system.
At the time of the inspection the inspectors could not read the digital display on the flow
monitor.
The inspection team then saw the Fournier rotary sludge presses. Facility staff stated that
these presses are expensive to operate and maintain. Two presses are operated at a time,
and they are rotated into operation each week (image 228-229). Sludge solids that leave
the Fournier press are put into a dumpster for disposal.
C. Records Review
Before the inspection the inspection team reviewed Facility records. These records
included:
NPDES Permit Number MA0100986, City of Fitchburg Wastewater
Treatment Facilities Commission effective September 1, 2010
Consent Decree United States and Massachusetts v. City of Fitchburg,
Filed 10/2/2012
Consent Decree Semi - Annual Progress Report Dated February 15, 2022
Wastewater Management Plan, submitted May 15, 2019
Wastewater Management Plan Phase II, submitted December 31, 2020
Records and notifications of SSO events
Records and notification of CSO events
D. Closing Conference
The inspection team thanked Facility personnel for their time and confirmed Mr.
McNamara as the primary point of contact for future communication. The inspection
team informed them that they would receive a copy of the inspection report in about 60
days. The Inspection Team departed at approximately 12 PM.
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Unless otherwise noted, this report describes conditions at the facility / property as
observed by EPA inspector(s), and / or through records provided to and / or information
reported to EPA inspector(s) by facility representatives and as understood by the
inspector(s). This report may not capture all operations or activities ongoing at the time
of the inspection. This report does not make final determinations on potential areas of
concern. Nothing in this report affects EPA's authorities under federal statutes and
regulations to pursue further investigation or action.
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