PES Process Description of Sequencing Batch Reactor System
SCREENING
Screening Pit (SP) for the first treatment step. A Bar Screen is installed in the Screening Pit to remove large solids such as metals, glass, wood and rags that may clog the process equipment downstream. The Bar Screen is provided with a manual rake arm for small treatment plants, and is upgraded to a fully automatic motorized model in large treatment plants. For the motorized model, the solids are continuously removed from the screen by the motorized rake arm and deposited in a solids compartment for offsite disposal.
EQUALIZATION TANK
As effluent discharge is always non-consistent in most cases, it is necessary to provide for a buffer tank to equalize this inconsistency. The Equalization Tank (EQT) is used to stabilize the variations in flow and effluent characteristics. This is achieved by providing sufficient retention time in the tank, and installing a mixing system to ensure uniform effluent quality at a predetermined flow volume. A coarse bubble diffuser grid is installed in the tank to provide air mixing. Air is supplied by an external air blower connected to the diffuser grid. The tank is also installed with submersible pumps with level switches to regulate the flow going into the next treatment step. Biodegradable solids are cut by the cutter blade impeller of the submersible pump when it is operating, thereby facilitating biological degradation of these solids further downstream.
SEQUENCING BATCH REACTOR
The Sequencing Batch Reactor (SBR) is an activated sludge process designed to operate under non-steady state conditions. An SBR operates in a true batch mode with aeration and sludge settlement both occurring in the same tank.SBRs produce sludge with good settling properties providing the influent wastewater is admitted into the aeration in a controlled manner. Controls range from a simplified float and timer based system with a PLC.
Aerated Fill
Mixed liquor is drawn through the manifold, mixed with the influent flow in the motive liquid pump, and discharged, as motive liquid, to the 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.
React
During this period aeration continues until complete biodegradation of BOD and nitrogen is achieved. After the substrate is consumed famine stage starts. During this stage some microorganisms will die because of the lack of food and will help reduce the volume of the settling sludge. The length of the aeration period determines the degree of BOD consumption.
Settle.
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.
Decant
This period is characterized by the withdrawal of treated effluent from approximately two feet below the surface of the mixed liquor by the fixed solids excluding decanter. This removal must be done without disturbing the settled sludge.
Idle
The time in this stage can be used to waste sludge or perform backwashing of the jet aerator. The wasted sludge is pumped to an anaerobic digester to reduce the volume of the sludge to be discarded. The frequency of sludge wasting ranges between once each cycle to once every two to three months depending upon system design.
CHLORINE CONTACT CHAMBER
Biologically-treated effluent shall then flow into the Chlorine Contact Chamber, wherein liquid chlorine is dosed inline to destroy pathogens in the effluent prior to discharge or reuse. The disinfected effluent maybe recycled as gray water for non-potable uses such as landscape irrigation and toilet flushing after installing a simple tertiary filtration system.
AEROBIC SLUDGE DIGESTER
Waste sludge is drained into the Aerobic Sludge Digester for further stabilization and volume reduction. Diffused air is supplied to the tank to provide oxygen for the metabolism and growth of resident microorganisms tasked with digesting the sludge.
Digested sludge may then be siphoned off by third party contractor for disposal offsite, or it maybe dewatered mechanically in a Filter Press Sludge Dewatering System. The sludge is dosed with polymer flocculant and passes through an inline static mixer to ensure homogenous mixing. It then flows to the Filter Press, wherein filter plates are filled up with the sludge slurry and pressed using a hydraulic pump. Filtrate are drained off and returned to the Equalization Tank for treatment. The filter plates are then separated to allow the pressed sludge cake to drop to the filter cake trough. Solids content in the sludge is increased to 30% after pressing, allowing the sludge cake to be placed in plastic bags and disposed offsite or mixed with soil as soil conditioner.
BIO-AUGMENTATION TREATMENT
A comprehensive wastewater treatment program aimed to enhance wastewater treatment parameters and reduce organic loading prior to its final treatment in a wastewater treatment facility which covers program from bacteria seeding for organic digestion to dosing of enzymes serving as catalyst in the biological treatment process. The design of this biological treatment system requires an understanding of the biological principles, kinetics of metabolism, principles of mass balance, and operations necessary to control the environment during the process.
BACTERIA SEEDING
The treatment starts by seeding the type of bacteria culture fit in the wastewater to be treated. Bacteria cultures are seeded in holding tanks such as grease traps, grease interceptors, lift stations and sump pits to achieve the required retention time efficient for the bacteria culture to reach the optimum condition and environment to multiply and biodegrade the incoming organic waste.
ENZYMES - THE CATALYST
The treatment also involves dosing of the required enzymes on the determined dosage points where bacteria cultures are seeded. These enzymes serve as catalysts in the biological process allowing the organic digestion to undertake at a faster rate. With the aid of enzymes, treatment of wastewater requires less retention time resulting to accommodation of a larger volume of wastewater to be treated by the wastewater treatment facility.
WATER SOFTENERS FOR COMMERCIAL AND INDUSTRIAL APPLICATIONS
All water supplies contain some amount of calcium and magnesium, commonly referred to as hardness. Hard water is undesirable for most commercial and industrial uses because of its tendency to form mineral scale, soap scum and chemical sludges. Water softeners utilize ion exchange resin to exchange the calcium, magnesium and other scale forming mineral scale, the process is referred to as water softening.
PHILGEN’s Water Softeners are commonly used in commercial and industrial applications to avoid scale formation, increase the efficiency of soaps and detergent and for chemical processing requirements. Typical applications include boilers, humidifiers, reverse osmosis feed water pretreatment, water heaters, cooling towers, car washers, laundries, hospitals, hotels, apartment complexes, resorts, beverage bottlers, plating shops, manufacturing plants and chemical processing industries.
PHILGEN’s Water Softeners are designed to provide years of trouble free service in demanding industrial and commercial applications. Fiberglass resin or mild steel epoxy coated resin tank are used for corrosion resistance and long life. High capacity ion exchange resin provides superior efficiency with minimal salt consumption. Cast iron diaphragm valves are included for reliability and corrosion resistance. Automatic or manual regeneration is available.
DESIGN FEATURES:
¨ Premium quality ion exchange resin provides exceptional capacity and hardness removal with excellent resin life. Resin meets FDA regulations and is approved by the US Department of Agriculture as well as BFAD. Epoxy coated mild steel tanks ASTM A36 for long-term durability, with an option for fiberglass composite tanks for corrosion resistance.
¨ Individual diaphragm or multi-port valves – flexible choices for automatic regeneration based on timer of flow meter.
¨ PVC flow meters – the meter initiates regeneration based on actual water use to reduce consumption (optional).
¨ Twin alternating systems – provide an uninterrupted supply of soft water. Series of softeners can be furnished as single, twin or triple systems with wide variety of alternator systems. Polyethylene brine tank with salt platform – eliminates corrosion and minimizes cleaning requirements.
¨ High flow distributors – two grades of gravel are combined with high flow distribution with low- pressure drop.
PES Process Description of a Conventional Activated Sludge System (CAS)

PES Process Description of a Conventional Activated Sludge System (CAS)
SCREENING CHAMBER
Raw sewage shall pass through the bar screen, wherein large solids are trapped on it and disposed offsite as solid waste.
EQUALIZATION
Raw wastewater is allowed to flow by gravity to the equalization, wherein varying concentration of pollutants and flowrate is homogenized or equalized. Homogenization is achieved through the introduction of air into the tank to create turbulence. This action likewise results in partial BOD removal of the waste stream by resident microorganisms.
COAGULATION (Optional)
Incoming wastes from equalization shall be diverted to the Coagulation Tank. Coagulation is the first step in breaking up the oil emulsion of the waste stream and promote the clustering of the solids and grease. Acidic coagulant chemicals such as Aluminum Sulfate or Polyaluminum Chloride (PAC) shall be dosed into the Coagulation Tank and mixed rapidly with the incoming wastes. This initiates the coagulation process, which chemically breaks down the oil emulsion and agglomerates the grease into loose clusters or lumps.
FLOCCULATION (Optional)
From the Coagulation Tank, the wastes shall flow into the Flocculation Tank. The next treatment step consists of dosing a flocculant chemical, usually an anionic polymer, to further enlarge the clusters and lumps formed earlier in the coagulation process. As the umps become bigger, it increases its settleability – in the case of the grease and other suspended solids, or floatability. Slow mixing is performed to avoid destroying the flocs being formed out of the coagulated lumps
The pH shall likewise be adjusted to a level suitable for discharge into the Sewage Treatment Plant (STP). A chemical metering pump shall dose caustic soda to neutralize the pH. A pH controller shall be installed to control the operation of the chemical metering pump and avoid overdosing of caustic soda. After pH adjustment, the wastewater containing metal precipitates are dosed with a coagulant such as aluminum sulfate or polyaluminum chloride (PAC). The coagulant enables the precipitates to agglomerate together forming microflocs. Suspended solids and oils likewise attached to these clusters. Air mixing is provided by an air blower.
INDUCED AIR FLOTATION
Induced Air Flotation (IAF) is a highly efficient process for removal of oils, greases and suspended solids, which is further enhanced by chemical flocculation. The IAF disc features a diffuser that incorporates fine holes near it perimeter for ultra-fine bubble diffusion into the liquid. The motor spins the unique diffuser disc, creating a low-pressure zone at disc’s diffuser ports. The disc draws air above the liquid surface, which then precedes down trough the draft tube, into the disc and out of the submerged diffuser ports. As each bubble exits trough a hole in the end of the diffuser disc, the spinning disc shears it into microscopic air bubble fragments measuring form 10-100 microns in diameter. These air bubbles adhere to minute solids such as oil and grease. The bubbles slowly rise to the surface around the unit, bringing the solids to the surface. The floated solids are then skimmed off by the scum skimmer, while the clear effluent flows under a weir towards the Aeration tank. The Induced Air Flotation System is expected to remove most of the oils and suspended solids, while having a significant impact on BOD reduction as well.
AERATION TANK
From the Induced Air Flotation, the treated effluent flows into the Aeration Tank in parallel operation, wherein aerobic and facultative bacterial culture is maintained in complete suspension. The activated-sludge process involves the production of an active mass of microorganisms capable of degrading organic
wastes in the presence of oxygen. The Aeration tanks are equipped with air blowers and fine bubble diffusers to provide the required oxygen for sustained bacterial growth and activity. Bacterial cells and inorganic matter formed during this activity shall form bioflocs that will settle in the Settling Tank.
A minimum mixed liquor suspended solids (MLSS) concentration shall be maintained to ensure the complete biodegradation of the estimated Biological Oxygen Demand (BOD) load. This is achieved by returning a portion of the sludge from the Settling Tank to the Aeration Tank. The purpose of the Return Activated Sludge (RAS) is to maintain a sufficient level of biomass in the Aeration Tank so that the required degree of treatment can be obtained in that time interval desired. The sludge recirculation rate may be increased or decreased depending on the influent BOD level, thus lending flexibility to the treatment in various field conditions.
SETTLING TANK
From the Aeration Tank, the mixed liquor overflows to the Settling Tanks in parallel operation for the separation of bioflocs from the supernatant. Efficient removal of these bioflocs from the wastewater shall result in a well-clarified stable effluent, which is in low BOD and suspended solids. A certain mean-cell residence time is maintained to enable the MLSS to form settleable bioflocs at the bottom hopper of the Settling Tank. A portion of the settled sludge at the hopper is recycled back to the Aeration Tank as seed biomass in order to maintain the required MLSS concentration. Less sludge volume is generated in this process, resulting in reduced sludge pumps out. Treated effluent shall be suitable for discharge to Class C waters.
AEROBIC SLUDGE DIGESTION
Excess sludge from the Induced Air Flotation and Settling Tank is further treated in the Sludge Digestion Tank where the endogenous phase of the microorganism occurs. In the Endogenous phase, the microorganisms are forced to metabolize their own protoplasm in the absence of sufficient nutrients. This results in a substantial reduction of the sludge volume as the surviving cells “digest” each other for sustenance.
CHLORINE CONTACT CHAMBER
Biologically-treated effluent shall then flow into the Chlorine Contact Chamber, wherein liquid chlorine is dosed inline to destroy pathogens in the effluent prior to discharge or reuse. The disinfected effluent maybe recycled as gray water for non-potable uses such as landscape irrigation and toilet flushing after installing a simple tertiary filtration system.
SCREENING CHAMBER
Raw sewage shall pass through the bar screen, wherein large solids are trapped on it and disposed offsite as solid waste.
EQUALIZATION
Raw wastewater is allowed to flow by gravity to the equalization, wherein varying concentration of pollutants and flowrate is homogenized or equalized. Homogenization is achieved through the introduction of air into the tank to create turbulence. This action likewise results in partial BOD removal of the waste stream by resident microorganisms.
COAGULATION (Optional)
Incoming wastes from equalization shall be diverted to the Coagulation Tank. Coagulation is the first step in breaking up the oil emulsion of the waste stream and promote the clustering of the solids and grease. Acidic coagulant chemicals such as Aluminum Sulfate or Polyaluminum Chloride (PAC) shall be dosed into the Coagulation Tank and mixed rapidly with the incoming wastes. This initiates the coagulation process, which chemically breaks down the oil emulsion and agglomerates the grease into loose clusters or lumps.
FLOCCULATION (Optional)
From the Coagulation Tank, the wastes shall flow into the Flocculation Tank. The next treatment step consists of dosing a flocculant chemical, usually an anionic polymer, to further enlarge the clusters and lumps formed earlier in the coagulation process. As the umps become bigger, it increases its settleability – in the case of the grease and other suspended solids, or floatability. Slow mixing is performed to avoid destroying the flocs being formed out of the coagulated lumps
The pH shall likewise be adjusted to a level suitable for discharge into the Sewage Treatment Plant (STP). A chemical metering pump shall dose caustic soda to neutralize the pH. A pH controller shall be installed to control the operation of the chemical metering pump and avoid overdosing of caustic soda. After pH adjustment, the wastewater containing metal precipitates are dosed with a coagulant such as aluminum sulfate or polyaluminum chloride (PAC). The coagulant enables the precipitates to agglomerate together forming microflocs. Suspended solids and oils likewise attached to these clusters. Air mixing is provided by an air blower.
INDUCED AIR FLOTATION
Induced Air Flotation (IAF) is a highly efficient process for removal of oils, greases and suspended solids, which is further enhanced by chemical flocculation. The IAF disc features a diffuser that incorporates fine holes near it perimeter for ultra-fine bubble diffusion into the liquid. The motor spins the unique diffuser disc, creating a low-pressure zone at disc’s diffuser ports. The disc draws air above the liquid surface, which then precedes down trough the draft tube, into the disc and out of the submerged diffuser ports. As each bubble exits trough a hole in the end of the diffuser disc, the spinning disc shears it into microscopic air bubble fragments measuring form 10-100 microns in diameter. These air bubbles adhere to minute solids such as oil and grease. The bubbles slowly rise to the surface around the unit, bringing the solids to the surface. The floated solids are then skimmed off by the scum skimmer, while the clear effluent flows under a weir towards the Aeration tank. The Induced Air Flotation System is expected to remove most of the oils and suspended solids, while having a significant impact on BOD reduction as well.
AERATION TANK
From the Induced Air Flotation, the treated effluent flows into the Aeration Tank in parallel operation, wherein aerobic and facultative bacterial culture is maintained in complete suspension. The activated-sludge process involves the production of an active mass of microorganisms capable of degrading organic
wastes in the presence of oxygen. The Aeration tanks are equipped with air blowers and fine bubble diffusers to provide the required oxygen for sustained bacterial growth and activity. Bacterial cells and inorganic matter formed during this activity shall form bioflocs that will settle in the Settling Tank.
A minimum mixed liquor suspended solids (MLSS) concentration shall be maintained to ensure the complete biodegradation of the estimated Biological Oxygen Demand (BOD) load. This is achieved by returning a portion of the sludge from the Settling Tank to the Aeration Tank. The purpose of the Return Activated Sludge (RAS) is to maintain a sufficient level of biomass in the Aeration Tank so that the required degree of treatment can be obtained in that time interval desired. The sludge recirculation rate may be increased or decreased depending on the influent BOD level, thus lending flexibility to the treatment in various field conditions.
SETTLING TANK
From the Aeration Tank, the mixed liquor overflows to the Settling Tanks in parallel operation for the separation of bioflocs from the supernatant. Efficient removal of these bioflocs from the wastewater shall result in a well-clarified stable effluent, which is in low BOD and suspended solids. A certain mean-cell residence time is maintained to enable the MLSS to form settleable bioflocs at the bottom hopper of the Settling Tank. A portion of the settled sludge at the hopper is recycled back to the Aeration Tank as seed biomass in order to maintain the required MLSS concentration. Less sludge volume is generated in this process, resulting in reduced sludge pumps out. Treated effluent shall be suitable for discharge to Class C waters.
AEROBIC SLUDGE DIGESTION
Excess sludge from the Induced Air Flotation and Settling Tank is further treated in the Sludge Digestion Tank where the endogenous phase of the microorganism occurs. In the Endogenous phase, the microorganisms are forced to metabolize their own protoplasm in the absence of sufficient nutrients. This results in a substantial reduction of the sludge volume as the surviving cells “digest” each other for sustenance.
CHLORINE CONTACT CHAMBER
Biologically-treated effluent shall then flow into the Chlorine Contact Chamber, wherein liquid chlorine is dosed inline to destroy pathogens in the effluent prior to discharge or reuse. The disinfected effluent maybe recycled as gray water for non-potable uses such as landscape irrigation and toilet flushing after installing a simple tertiary filtration system.
COMPANY HISTORY
PHILGEN ENGINEERING SERVICES is a company that consists of a group of engineers and technical people with previous training and hands-on experiences on water and wastewater treatment design, plant construction, environmental management and pollution control.
We provide total environmental solution ranging from conceptual system design, detailed engineering design, supply and installation, testing and commissioning, training of operators, as well as operation and maintenance services.
PHILGEN serves industries, which includes manufacturing plants, hospitals, office buildings, foods, textiles, and hotels.
The company aims to be competitive and reliable contractor in the following areas:
§ Water Treatment System
- Boiler Maintenance Chemicals: Scale/Corrosion Inhibitor, Oxygen Scavenger, Condensate Line Corrosion Control, Descaler
- Cooling System Chemicals: Scale/Corrosion Control, Algaecide, Fungicide, Descaler, AHU Coil Cleaner, Corrosion Control, Dispersant
- Filtration Systems: Sand filter, Multi-media filter, Activated Carbon Filter, Cartridge filter
- Softener System
- Deionizer/Demineralizer Systems: Single-Bed system, Dual-Bed system, Mixed-Bed system
- Chemical Feed Pumps
- pH/Conductivity Controller
- Degasifier
- Chlorination System
§ Wastewater Bio-chemical Treatment: Supply of Bacteria, Enzymes, Flocculants, Polymers Wastewater Treatment System
- , Coagulants, Disinfectants, Trickling Filters
- Complete Sewage Treatment Plant: Conventional Activated Sludge (CAS), Sequencing Batch Reactor (SBR), Biofilm Process (BP)
- Industrial Wastewater Treatment Plant: Chemical Treatment,
Dissolved Air Flotation (DAF), Inclined Plate Clarifier (IPC), Oil Water Separator (OWS)
- Sludge Dewatering System: Filter Press, Sludge Drying Bed
Belt Press and Centrifuge
§ Plumbing Works: Design and Installation of Complete Piping Systems, Preventive Maintenance
§ Electrical Works: Design and Installation of Complete Electrical Systems
§ Fire Protection System: Design and Installation of complete sprinkler system, fire hydrant and fire pump system.
§ Mechanical Works: Design and Installation of Aircondition system, ventilation, Duct Work, Ice Plant and Cold Storage, Air Scrubber, Cooling Towers.
§ Preventive Maintenance Chemicals
- Janitorial Cleaning Chemicals: Non-buffable Wax, Emulsion Wax, Floor Sealer, Floor Stripper, Liquid Marble Crystallizer, Disinfectant Cleaner, Glass Cleaner, Odor Eliminator, Exhaust hood cleaner, Spray Buffing Solution, Air freshener, Carpet Cleaner, Liquid Hand Soap
- Equipment Maintenance Chemicals: Lubricants, Penetrating Oil, Grease, Deruster, Contact Cleaner
We provide total environmental solution ranging from conceptual system design, detailed engineering design, supply and installation, testing and commissioning, training of operators, as well as operation and maintenance services.
PHILGEN serves industries, which includes manufacturing plants, hospitals, office buildings, foods, textiles, and hotels.
The company aims to be competitive and reliable contractor in the following areas:
§ Water Treatment System
- Boiler Maintenance Chemicals: Scale/Corrosion Inhibitor, Oxygen Scavenger, Condensate Line Corrosion Control, Descaler
- Cooling System Chemicals: Scale/Corrosion Control, Algaecide, Fungicide, Descaler, AHU Coil Cleaner, Corrosion Control, Dispersant
- Filtration Systems: Sand filter, Multi-media filter, Activated Carbon Filter, Cartridge filter
- Softener System
- Deionizer/Demineralizer Systems: Single-Bed system, Dual-Bed system, Mixed-Bed system
- Chemical Feed Pumps
- pH/Conductivity Controller
- Degasifier
- Chlorination System
§ Wastewater Bio-chemical Treatment: Supply of Bacteria, Enzymes, Flocculants, Polymers Wastewater Treatment System
- , Coagulants, Disinfectants, Trickling Filters
- Complete Sewage Treatment Plant: Conventional Activated Sludge (CAS), Sequencing Batch Reactor (SBR), Biofilm Process (BP)
- Industrial Wastewater Treatment Plant: Chemical Treatment,
Dissolved Air Flotation (DAF), Inclined Plate Clarifier (IPC), Oil Water Separator (OWS)
- Sludge Dewatering System: Filter Press, Sludge Drying Bed
Belt Press and Centrifuge
§ Plumbing Works: Design and Installation of Complete Piping Systems, Preventive Maintenance
§ Electrical Works: Design and Installation of Complete Electrical Systems
§ Fire Protection System: Design and Installation of complete sprinkler system, fire hydrant and fire pump system.
§ Mechanical Works: Design and Installation of Aircondition system, ventilation, Duct Work, Ice Plant and Cold Storage, Air Scrubber, Cooling Towers.
§ Preventive Maintenance Chemicals
- Janitorial Cleaning Chemicals: Non-buffable Wax, Emulsion Wax, Floor Sealer, Floor Stripper, Liquid Marble Crystallizer, Disinfectant Cleaner, Glass Cleaner, Odor Eliminator, Exhaust hood cleaner, Spray Buffing Solution, Air freshener, Carpet Cleaner, Liquid Hand Soap
- Equipment Maintenance Chemicals: Lubricants, Penetrating Oil, Grease, Deruster, Contact Cleaner
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