Town of Basics
Sewage Treatment Town
of The Town of The treatment plant receives wastewater from the
1.
120 septic tank effluent pump systems 2.
Fluidyne
ISMATM Sequencing Batch Reactor 3.
Geoflow
wasteflow® drip irrigation system The
wastewater treatment plant has a designed hydraulic capacity of 60,000 gallons
per day (GPD). The treatment plant is currently operating at approximately 20%
of its capacity. The
treatment plant is currently operating under a Conditional Operating Permit
issued by the Virginia Health Department (Permit number 02-100-0070). A final
Operating Permit will be issued after the conditions of operation have been met
by the Town of Why is Sewage Treatment Important? Effective
sewage treatment prevents a variety of ailments that can be spread by exposure
to pathogens that can be present in untreated sewages, and thus helps prevent
disease. Discharges of untreated sewage can contaminate groundwaters and
surface waters used for drinking, recreation, and fish and shellfish fisheries.
General Principles of Sewage Treatment Raw
sewage and septic wastewaters contain a variety of contaminants.
Most
sewage treatment technologies operate by combining basic physical, chemical,
and biological processes. Primary
Treatment (Anaerobic Selector Chamber) Primary treatment (Influent
chamber) removes solid chunks and particles from raw sewage through gravity
separation. The partially-treated liquid discharged from primary treatment is
called primary effluent. The influent chamber utilizes anaerobic digestion as
the first treatment process at the Exmore Wastewater Treatment Plant Anaerobic Digestion of Sewage The treatment
of sewage is largely a biochemical operation, where chemical transformations of
the sewage are carried out by living microorganisms. Different environments
favor the growth of different populations of microorganisms and this in turn
affects the efficiency, end products, and completeness of treatment of the
sewage. Sewage treatment systems, whether they are standard septic systems or
more advanced treatment technologies, attempt to create specific biochemical
environments to control the sewage treatment process is based on the type of
biochemical transformation that occurs. Three basic
types of biochemical transformations occur as sewage is treated. 1ST - The removal of soluble organic matter. This is composed of
dissolved carbon compounds such as detergents, greases, and body wastes, which
make up much of the BOD content of the sewage. 2ND- The
digestion and stabilization of insoluble organic matter. These are the sewage
solids, such as body wastes and food particles, which make up the remainder of
the BOD. 3RD - The
transformation of soluble inorganic matter such as nitrogen and phosphorus. The two major
biochemical environments in which sewage treatment is carried out are termed anaerobic and aerobic environments. anaerobic
environment
is one in which dissolved oxygen is either not present or its concentration is
low enough to limit aerobic metabolism. aerobic
environment
is one in which dissolved oxygen is available in sufficient quantity that the
growth and respiration of microorganisms is not limited by lack of oxygen. The
biochemical environment has a profound effect upon the ecology of the microbial
population which treats the sewage. Anaerobic
conditions favor the growth of primarily bacterial populations and produce a
different variety of end products; Aerobic
conditions tend to support entire food chains from bacteria up to rotifers and protozoas.
These microbes breakdown organic matter using many metabolic pathways based on
aerobic respiration with carbon dioxide as the main end product. Solids in
sewage contain large amounts of readily available organic material that would
produce a rapid growth of microorganisms if treated aerobically. Anaerobic
decomposition is able to degrade this organic material while producing much
less (approximately one-tenth) biomass than an aerobic treatment process. The
principal function of anaerobic digestion is to stabilize insoluble organic
matter and to convert as much of these solids as possible to end products such
as liquids and gases (including methane) while producing as little residual
biomass as possible. It is for this reason that sewage treatment in a
conventional septic tank is designed to be an anaerobic process. Organic matter
treated anaerobically is not broken down to carbon dioxide; final end products
are low molecular weight acids and alcohols. These may be further
converted anaerobically to methane or, if sent to an environment (such as the
leaching field) where aerobic bacteria are present, further broken down to
carbon dioxide. Anaerobic digestion of organic matter is also a much slower
process than aerobic digestion of organics and where rapid digestion of organic
matter is needed an aerobic treatment process must be used. As discussed
above, an anaerobic environment is also necessary for denitrification, as the
bacteria which carry out this process require anaerobic conditions to reduce
nitrate to nitrogen gas. Many nitrogen-removal technologies are designed to
provide an anaerobic treatment chamber as part of the treatment process. Aerobic Treatment of Sewage As the name
implies, this process utilizes aerobic bacteria to break down sewage. The
principal advantage of aerobic sewage treatment is its ability to rapidly and
completely digest sewage, reducing BOD to low levels. This process is used
primarily to reduce BOD and, in systems that remove nitrogen, to nitrify the
waste so that it can later be denitrified. Because the BOD in raw sewage is
usually high, and available oxygen is rapidly consumed by the sewage, most
aerobic treatment units are designed to supply supplemental oxygen to the
sewage to keep the treatment process aerobic. The activated sludge process is similar to suspended culture in
that it also utilizes the resident population of bacteria in the solids and
sludge in the treatment unit, again, usually by mixing of the sewage so that
the bacteria are kept in suspension. In the activated sludge process, however,
there are usually periods where mixing ceases and the solids are allowed to
settle. It is then assumed that the sludge will become anaerobic and the
anaerobic bacteria in the sludge will denitrify the waste. This is the
principle used by batch reactors.
As the name implies, batch reactors treat sewage in batches. A batch of sewage
is allowed to settle so that solids are removed; the batch of sewage is then
aerated and mixed and then allowed to settle for a period of anaerobic
treatment (this process may be repeated several times on the same batch). When
treatment is complete, the finished batch of sewage is pumped out and the next
batch enters the unit to begin treatment. The Town of
1.
Anaerobic
Chamber 2.
Surge/Anoxic/Mix
(SAM) Chamber 3.
Sequencing
Batch Reactor (SBR) Chamber 4.
Jet
Aeration 5.
Recycle
Line 6.
Decanter Sequencing Batch Reactor A sequencing batch reactor is a modified conventional
continuous-flow activated sludge treatment system. The modified conventional
activated sludge systems treat wastewater in a series of separate tanks.
Sequencing batch reactors carry out aeration and sedimentation/clarification
simultaneously in the same tank. They are designed for the removal of
biochemical oxygen demand (BOD) and total suspended solids (TSS) from typical
municipal and industrial wastewater at flow rates of less than 5 MGD.
Modification to the design of the basic system allows for nitrification and
denitrification and for the removal of biological phosphorus to occur. The sequencing batch reactor is particularly suitable for small
flows and for nutrient removal. Sequencing batch reactors can be either used
for new developments or connected to existing septic systems. Small reactors
can be sited in areas of only a few hundred square feet. While sequencing batch
reactor cost and operation and maintenance requirements are greater than those
for conventional On-site
Sewage Disposal System (OSDS),
sequencing batch reactors may be suitable alternatives for sites where
high-density development requires adequate treatment of wastewater effluent. The operating principles of a batch activated sludge process, or
SBR, are characterized is five (5) discrete periods: 1.
Anoxic Fill 2.
Aerated Fill 3.
React 4.
Decant Anoxic Fill The influent wastewater is distributed throughout the settled sludge through the influent distribution manifold to provide good contact between the microorganisms and the substrate. The influent can be either pumped in or allowed to flow in by gravity. Most of this period occurs without aeration to create an environment that favors the reproduction of microorganisms with good settling characteristics. Aeration begins at the beginning of this period.
Mixed liquor is drawn through the manifold, mixed with the
influent flow in the motive liquid pump, and discharged, as motive liquid, to
the jet aerator. This initiates the feast period. Feast is when the
microorganisms have been in contact with the substrate and a large amount of
oxygen is provided to facilitate the substrate consumption. Nitrification and denitrification
occurs at the beginning of this stage. This period ends when the tank is either
full or when a maximum time for filling is reached. Aeration is discontinued at this stage and solids separation takes
place leaving clear, treated effluent above the sludge blanket. During this
clarifying period no liquids should enter or leave the tank to avoid turbulence
in the supernatant.
This period is characterized by the withdrawal of treated effluent
from approximately two feet below the surface of the mixed liquor by the
floating solids excluding decanter. This removal must be done without
disturbing the settled sludge. 1. Equalization, biological treatment, and
secondary clarification can be achieved in a single reactor vessel 2. Operating
flexibility and control 3. Minimal
footprint 4. Potential
capital cost savings by eliminating clarifiers and other equipment The performance of SBRs is typically comparable to conventional
activated sludge systems. Depending on their mode of operation, SBRs can
achieve good BOD and nutrient removal. For SBRs, the BOD removal efficiency is
generally 85 to 95 percent. SBR manufacturers will typically provide a process
guarantee to produce an effluent of less than; 2. 10 mg / L TSS 3. 5 - 8 mg / L TN 4. 1 - 2 mg / L TP Geoflow Drip Irrigation Drip
irrigation (sometimes called trickle irrigation) works by applying water slowly,
directly to the soil. The high efficiency of drip irrigation results from two
primary factors. The first is that the water soaks into the soil before it can
evaporate or run off. The second is that the water is only applied where it is
needed, (at the plant's roots) rather than sprayed everywhere. Drip systems are
simple and pretty forgiving of errors in design and installation. This technology is a
specific application of Pressurized Leach Field Dosing. From the dosing tank,
filtered effluent is distributed close to the surface of the ground, through
small plastic tubing with holes every one or two feet. Leachate is
preferentially taken up and processed by the surface planting, and
evapotranspiration is a significant factor. According to the National Small
Flows Clearing House (NSFCH), which uses the term Low Pressure Pipe (LPP) for
this system, it originated in Drip
"irrigation" is the shallow, slow, pressure-dosed release of
pretreated wastewater directly at or above the surface of the soil. Common to
all pressurized dosing systems is the uniform distribution of effluent and
periodic dosing and resting cycles. Particular to drip irrigation or LPP
systems is the use of small diameter piping with underground drip emitters
placed about 6" under the surface. Effluent must be treated and filtered before
distribution. Effluent is applied at a controlled rate in the plant root zone,
which tends to minimize percolation and enhance evapotranspiration (the
evaporation of water from soils, plants and surface waters). The level controls
in the dosing chamber are set for a specific pumping sequence, depending on the
design, which might be as seldom as once a day. The laterals are placed in
narrow trenches that allow enough storage volume so that the depth of the
wastewater does not exceed 2 or 3 inches of the total trench depth during each
dosing cycle. Hydraulic loading rates may vary between 0.01 and 0.4 gallons per
day per square foot. Below is schematic of a Drip Irrigation System.
Process monitoring There have been several quality control processes employed by the
Town of 2.
Daily
monitoring of the Wastewater Treatment Plane has been established. 3.
Emergency
call-in procedures have been established. The automatic dial system will
contact 3 key personnel and will contact the Northampton County Sheriffs
Department. The system is setup to call if there is an alarm indicating a
problem. 4.
Operator is
on duty 5 days per week. 5.
A contact
person has been established to call for any technical assistance that should
arise. 6.
Several
daily work sheets have been prepared to record all information. Attached are
the current work sheets. | |||||||||||||||||||||||||||||