Cumberland
County Utilities Authority
Bridgeton, New Jersey
The Cumberland County Utilities Authority (CCUA) Wastewater Treatment
Plant (WWTP) has served as a sewage treatment center since the late 1800's.
In May of 1979 the CCUA opened a 7 MGD WWTP and today is the largest
user of the Cohansey River Basin.
The plant is a secondary treatment design with, flow equalization,
primary & secondary clarifiers, two 1.5 MGD aeration tanks, and sodium
hypochlorite disinfection. Solids are processed by anaerobic digestion
involving one primary digester and one two stage secondary digester.
The final disposal of sludge from the plant is by incineration used
only at certain times of the year and by land application. Sludge residuals
applied to land are tested to strict standards set forth by the NJDEP
and EPA, once tested and approved are classified as beneficial biosolids.
The CCUA applies biosolids with a specially designed truck through subsurface
injection. Farms use CCUA biosolids do so for their effective soil conditioning
benefit in growing sod, nursery stock, and grains.
The NJDEP biosolids land application program is in some ways more stringent
than the federal requirements set by the EPA.
Biosolids can only be applied through the strict guidelines set forth under
the direction of the New Jersey Department of Agriculture's Agricultural Management
practices and right-to-farm requirements.
Application require's individual site review and official documentation
from the NJDEP which must state Land Application Management Approval.
Additional requirements can be added at any time by the department
to a permit based on review of the residuals being applied to the land.

Pictured is the CCUA specially designed truck, subsurface injecting Biosolids.
Due to the success of the Biosolids program and BAE, the
CCUA received the EPA National First Place Award for "The Beneficial
Reuse of Biosolids".
The CCUA began using BAE in their primary anaerobic digester because
they were having difficulty maintaining the minimum volatile solids destruction
(VSD) of 38% required by the NJDEP for land applying sludge.
These problems also affected the methane production within the digester,
causing the plant to rely on their local natural gas supplier to provide
energy for operating the boilers to heat the digester as well as the
boilers responsible for heating the administration building.
Methane production from anaerobic digestion requires proper pH and
reliable organic matter to promote maximum methane production. When these
two issue were examined it appeared that both were in good order.
The boilers were checked and temperature of the biomass in the digester
was monitored. This was done because methane producing bacteria are extremely
sensitive to temperature change and a swing of 20°F can cause a 50%
loss in methane production and as little as a 5°F swing can inhibit
methane formers enough to cause acid accumulation, foul odor, and possible
digester failure.

750,000 Gallon Primary Digester
After completing several evaluations of the primary digester it became
evident that there was a breakdown in the two-part process involved in
the anaerobic digestion.
It appeared from the operation of the digester that the first phase
of digestion was taking place. The biomass was being broken down into
simple organic compounds by the acid-forming bacteria.
It was the second phase that was having difficulty responding to the
environment. It was in this phase that the acid forming bacteria seemed
to dominate the methane-forming bacteria,
causing a break down in methane production and creating a foul acid type odor.
BAE was added to the digester at the rate of 3 gallons per day. Within
90 days the odor was eliminated and methane production was at its maximum
production, creating more gas then the demand required; the digester
had recorded VSD levels as high as 62% and began to level off at a VSD
of 55%.
BAE had clearly demonstrated that a balance between the acid formers
and methane formers had been created and a stimulating effect was taking
place within the primary digester, improving the performance of the two-stage
secondary digester. Dewatering by the plants centrifuge machine improved,
receiving digested sludge as high as 6% creating a dewatered cake at
25 to 28%.
The CCUA made the decision to change the dewatering process from centrifuge
to gravity belt thickening. This process required polymers to be added
at the influent of the gravity belt and some of this material worked
its way into the primary digester.
Polymers used in this operation were toxic to the methane formers, causing
a loss of gas and excess volatile fatty acids and the odors associated
with them. BAE was increased to compensate for the problem; within 120
days the problem was eliminated and today the primary digester operates
at a VSD of 55 and higher and the rate of BAE treating the digester has
been reduced to 2.8 gallons per day.
Because of the success experienced in the primary digester it was decided
to treat the aeration tanks with BAE as well.
From the day the plant went on line the organic loading averaged 675
mg/l BOD and for several years it experienced high levels of TSS and
BOD in the effluent; many remedies had been tried to eliminate the problem.
BAE was added to each 1.5 MG aeration tank at the rate of 1.5 gallons.
Within 30 days the TSS BOD levels began drop; now both are both below
10 mg/l daily.
As we have seen many times before from the use of BAE the biomass activity
increases within the aeration tank, and mixed liquor levels are now lower
then ever before. As a result of this efficiency from the addition of
BAE, the CCUA has taken one of it's 1.5 MG aeration tanks out service.

Pictured is one of two 1.5 MG aeration tanks with air supplied by fine bubbling
diffusion. Following six months of treatment with BAE to both aeration tanks,
one of the two tanks was removed from service.
Stimulation of microbial growth due to the treatment of BAE in anaerobic
and aerobic environments has been shown again. These benefits help WWT
and have greatly contributed to the clean up of our waterways.
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