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Water's unique Characteristics and its essential Role for all life have inspired myths and influenced cultures, religions, art, and literature through all times.
The process involved for the RBC Biological Treatment method is named as FIXED FILM ROTATING BIOLOGICAL CONTACTOR BIOWHEELS. In this process by means of rotation of the bio wheels micro - organisms are expected to growth in the RBC and the overflow from the Lamella clarifier will be the first stage of the treated water. The micro organisms will develop on the surface of the disk and the colonization of the organisms will take place because of the inlet load into the system. The thick film like formation in the surface of the disk is the indication of the growth. In Sewage water the main constituents of Pollutants being organic in nature these can be digested easily in the RBC.
Sewage is created by institutions, residences, and hospitals and commercial and industrial establishments. Raw influent of sewage wastewater includes household waste liquid from the toilets, sinks, showers, kitchens, baths, and so forth that is disposed of sewage waste water.
The aim of the project is to Analysis of water consumption and power consumption of sewage treatment plant.
* To Analysis the water and power consumption of the sewage treatment plant
* To vary the parameters of water source, power source.
* To Analyze the Rotating Biological contactor Biowheels.Lamella clarifier
* Analyzing 2D design of the Sewage Treatment Plant.
* To analyze the results and propose appropriate solution.
Waste water collected from domestic and industrial communities must be returned to receiving waters or to the land. Although the collecting of storm water and drainage dates from ancient times the collection of waste water can be traced only to the early 1800s. The systematic treatment of wastewater followed in the late 1800s and early 1900s.
There are many methods and processes to treat wastewater. The most common approach uses primary treatment (screening and clarification) to remove solids; aerobic, suspended growth, activated sludge secondary treatment to reduce organic pollutants; and chlorine disinfection to reduce pathogens. Secondary treatment is the largest energy consumer (30 to 60% of total plant usage), followed by pumping and sludge processing. Although suspended growth, activated sludge is the most common wastewater treatment process, it is not the most energy efficient.
Aerated lagoons, trickling filters and rotating biological contactors are significantly more efficient. They are not as widely used because aerated lagoons require a large land area, and trickling filters and rotating biological contactors are better suited for smaller capacity applications. Many wastewater treatment plants are shifting from chlorine-based disinfection to UV disinfection to eliminate the risk of storage and handling of toxic chemicals. Although UV disinfection is energy intensive, it adds no chemical residue to the effluent. This feature is particularly important for discharge to sensitive aquatic environments or for wastewater reuse. In general, low pressure UV systems are substantially more efficient than medium pressure systems.
Energy efficiency opportunities in wastewater treatment include the use of fine bubble diffusers, dissolved oxygen control of aeration, high efficiency blowers, variable frequency drives on pumps and blowers, premium efficiency motors, and the reduction of the head against which pumps and blowers operate. Sewage is generally a mixture of domestic of waste water from bath, sinks and washing machines and toilets, waste water from all industry and rainwater runoff from roads and other surfaced areas.
Every day in the UK about 347,000 Kilometers of sewers collect over 11 Billion liters of waste water. This is treated about 9000 sewage treatment works before the treated effluent is discharged to inland waters, estuaries and the sea.
Without suitable treatment, the waste water we produce every day would damage the water environmental and creates to affect the public health problems. Untreated sewage contains organic matter carbohydrates, fats and proteins, bacteria and chemicals. Bacteria naturally present in environmental waters do break these substances down, but in doing so they use the oxygen dissolved in this water. If there were large or continuous untreated discharges of urban waste water the result could be too little oxygen for fish and other aquatic life to survive. So the purpose of waste water treatment is to remove organic substances to protect the environment from these effects. Sewage works therefore reproduce what would be occurring in the environmental. Settling out much of the solid matter is called Primary Treatment, and using Bacteria that digest and break down the organic substances is called Secondary Treatment.
Sometimes further treatment Tertiary is required to protect sensitive water environments; Tertiary treatment can involve disinfecting the treated effluent to protect the bathing and shellfish waters. It can also involve the removal of phosphorous or nitrates nutrients present in sewage. To protect the waters that is threatened by eutrophication. (ref sewage treatment in the UK defray department for environment food & Rural affairs,PB 6655 March 2002.).
Municipal water use is generally divided into four categories,
1. Domestic water normally used for sanitary and general purposes
2. Industrial water used for nondomestic purposes,
3. The Public service water normally used for fir fighting, and system maintenance and also municipal landscape irrigation.
4. Unaccounted for system losses and leakage
The following data are typical municipal water use in the United States Report.
( (George Tchobanoglous and Franklin L. Burton, 1991)
Domestic water use encompasses the water supplied to residential areas ,and commercial districts, institutional facilities, and recreational facilities as a measured by individual water meters .The uses to which this water is put include drinking, washing, bathing, culinary, and waste removal, and yard watering these kind of water collected from household sewage. Using the average flow values reported in above table of the water used in a municipal water supply system is for domestic purposes.
The water normally used by residential households consists of water for interior use such as showers and toilets and water for exterior use such as lawn watering and car washing, the household wastewater mostly used in sewage treatment plant. Typical data for interior water use are presented in below table.
How much amount of water used in residential areas water use for exterior applications varies widely depending upon the geographic location, climate and time of year and mainly consists of landscape irrigation.
The Residential areas 100% of water normally used by typical distribution of residential interior water use the following table given details
(George Tchobanoglous and Franklin L. Burton, 1991)
The water used by commercial facilities for sanitary purposes will vary widely depending on the type of activity means example of offices and compared to a restaurant. Typical water use values for various types of commercial facilities are reported in following table also for large commercial water using facilities such as laundries and car washes, careful estimates of actual water use should be made.
(George Tchobanoglous and Franklin L. Burton, 1991)
Water used by facilities such as hospitals, schools and rest home is usually based on some measure of the size of the facility and the type of housing function provided example of per student or per bed, and water normally use for schools will vary significantly depending on whether the students are housed on campus or are day students. The representative water use values for institutional facilities are reported following table.
(George Tchobanoglous and Franklin L. Burton, 1991)
The recreational facilities mostly water used in such as swimming pools, bowling alleys, and camps, resorts, then country clubs perform a wide range of functions involving water use. The following table typical water use values are reported.
Table: Typical water-use values for recreational facilities
(George Tchobanoglous and Franklin L. Burton, 1991)
Sewage treatment plant there are two main types of biological reaction, depending upon the presence or absence of free oxygen, the aerobic reaction takes place only in the presence of free oxygen and produces stable, relatively inert end products. Anaerobic reaction are more complex, being two stage, proceeding relatively slowly and leading to end products which are unstable and which still contain considerable amounts of energy. In any biological reaction the energy in the organic matter, used as food by the microorganisms, is split three ways; some is used in creating new microorganisms, some is incorporated in the end products of the reaction, the proportions of energy in the three areas depend upon the nature of the reaction, the type of organic matter, the type of microorganisms,and environmental conditions. The organic matter in wastewater thus provides the well as providing the energy for the oxidation reactions which releases the end products of biological treatment. (THY Tebbutt,1990).
Domestic sewage satisfies all these requirements but some industrial wastewaters may be lacking in nutrients or other factors, which could result in inhibition of biological activity, Toxic substances present in the wastewater can also mean that biological treatment of an organic wastewater is ineffective, although it is sometimes possible for microorganisms to become acclimated to substances which initially appear to be toxic. The aim of conventional biological treatment processes is to achieve almost complete removal of the organic matter in the feed. The activated sludge system is a common form of dispersed growth reactor, and both systems require a settling facility to remove the excess biological solids produced in the process. In the case of fixed film systems the solids are essentially dead cells, but with the dispersed growth activated sludge systems the bulk of the cells are living and are returned to the reactor for re use, only the excess solids being removed. (THY Tebbutt,1990).
Characterstics of waste water sewage treatment plant:
Â· Bio chemical oxygen demand
Â· Total dissolved solids
Â· Chemical oxygen demand
Â· Total suspended solids
Â· Bio chemical oxygen demand:
It is a measure of the amount of oxygen that bacteria will consume while decomposing organic matter under aerobic conditions.
Â· Total dissolved solids:
It comprises inorganic salts and small amounts of organic matter that are dissolved in water. The principle constituents are usually the captions , calcium, magnesium, sodium, and potassium and the anions carbonate, bicarbonate, chloride, sulphate and particularly in groundwater nitrate.
Â· Chemical oxygen demand:
It is a measure of the total quantity of oxygen required to oxidize all organic material into carbon dioxide and water.
* Total suspended solids:
It is a measure of the suspended solids in waste water, effluent, or water bodies determined by tests for "Total suspended non-filterable solids".
It is a measure of the acidity or alkalinity of a solution numerically equal to 7 for neutral solutions increasing with increasing alkalinity and decreasing with increasing acidity. The PH scale commonly in use ranges from 0 to 14. ( www.answers.com )
Classification of Waste Water Treatment Methods
The wastewater treatment is contaminants are removed by physical, chemical and also biological methods. Sewage Treatment Plant individual methods usually are classified as a physical unit operations, chemical unit operations and also Biological unit operations and processes. Although these operations and processes occur in a variety of combinations in Treatment Systems. (George Tchobanoglous, FranKlin L.Burton, 1991,1979,1972)
The Treatment methods in which the application of physical forces to predominate are known as physical operation unit. Because most of these methods involved directly from the first observations of a nature, and they were the first to be used for wastewater .treatment.
These are the Screening, Mixing, Flocculation, Flotation,sedimentation,Filtration,and Gas transfer are typical unit operations. (George Tchobanoglous, FranKlin L.Burton, 1991,1979,1972).
The first off all unit operation entered in wastewater treatment plants is screening .a screen is a device with openings ,generally of uniform a size, that is using to retain the coarse solids found in wastewater.
The screening elements may consists of parallel bars, wires or ,grating, rods, mesh, or perforated plate ,a screen composed of parallel bars or rods is called a bar rack sometimes called a bar screen).
The term screen is used for screening devices consisting of perforated plates wedges wire elements and wire cloth. The materials removed by these devices are known as screenings.
In Wastewater treatment, bar racks are used to protect the Pumps pipelines valves and other appurtenances from the damaged or clogging by a rags and large objects.
Sewage treatment plant is widely used to Barscreening,early screens were of the inclined disk or drum type, whose screening media consisted of bronze or copper plates with milled slots ,and were installed in place of sedimentation tanks for primary treatment .since the early 1970s,there has been resurgence of interest in the field of wastewater treatment in the use of screens of all types ,the application range from primary treatment to the removal of the residual suspended solids from biological treatment processes. (George Tchobanoglous, FranKlin L.Burton, 1991,1979,1972)
Mixing is an important unit operation in many phases of wastewater treatment including (1)the mixing of one substances completely with another, (2)the mixing of liquid suspensions,(3)the blending of miscible liquids,(4)flocculation and (5)heat transfer .chemicals are also mixed with sludge to improve tidal watering characteristics. In anaerobic digestion, mixing is used accelerate the biological conversion process and to heat the contents of the digester uniformly .
Most mixing operations in wastewater can be classified as continuous rapid or continuous. Continuous -rapid mixing is used most often where one substance is to be mixed with another. Continuous mixing is used where the contents of reactor or holding tank or basin must be kept in suspension.
Energy dissipation mixing:
The power input per unit volume of liquid can be used as a rough measure of mixing effectiveness, based on the reasoning that more input power creates greater turbulance,and greater turbulence leads to better mixing.
It is one of the most widely used in waste water treatment, sedimentation is the separation from the water, by gravitational settling, of suspended solids that are heavier than water, it is one of the most widely used unit operations in wastewater treatment .A Sedimentation basin may also be referred to as a sedimentation tank, settling basin ,or settling tank,
Sedimentation is used for grit removal, particularly floating matter removal in the primary settling basin, biological float removal in the activated sludge and settling basin and chemical flog removal. Whenever' the chemical coagulation processes is used.
Sewage treatment plant is widely used to chemical unit processes ,This Treatment Methods in which the removal or conversion of the contaminants is brought about by the chemicals or by other chemical reactions are known as a chemical processes unit. There are three different types chemical processes used in the wastewater treatment.Precipitation,and disinfection and adsorption, which the process mostly used in the wastewater treatment. In the chemical precipitation ,treatment is also accomplished by producing a chemical precipitate that will settle. In most cases the settled precipitate will contain the both constituents that may have reacted with the adding to chemicals and the substance that were swept of wastewater as the predicated settled in the water. (George Tchobanoglous, FranKlin L.Burton, 1991,1979,1972)
The settlement of fine colloidal and suspended solids can be assisted by the use of flocculation as but with dilute suspensions, such as lowland river waters, the opportunities for collisions and agglomeration are limited. In such circumstances flocculation does not significantly improve the settling characteristics of the suspension. the addition of a chemical coagulant, which precipitates flocculent solids in the water, followed by flocculation and sedimentation, can provide a high degree of clarification. the processes of chemical coagulation is thus carried out in a sequence of operations, the first of which involves rapid to permit enmeshment of the colloidal solids in the rapidly precipitating flock. (THY Tebbutt, 1990)
Following the initial stage precipitation stage, the suspension is passed to flocculation and sedimentation units, which may be separate or combined. the most popular coagulant for potable water treatment is aluminum sulphate, often referred to as alum. When it is added to water in small doses of around 20-50mg/l,a reaction takes place with the natural alkalinity present, and insoluble aluminum hydroxide is formed. this responds well to controlled flocculation. The chemical reactions which occur are complex but may be simplified as
Al2(SO4)3 +3Ca(HCO3)2 = 2Al(OH)3 + 3CaSo4 +6CO2
When using the commercial alum which has 16-18 molecules of water of crystallization, and expressing alkalinity in terms of calcium carbonate, each mg/l of alum reacts with 0.5mg/l of alkalinity. By using a range of coagulant does and PH values ,it is possible to determine the optimum conditions to achieve the required water quality. (THY Tebbutt, 1990)
In essence ,chemical precipitation depends upon the use of an added reagent which combines with the impurity to be removed to give an insoluble product which can then be removed by sedimentation, preceded by flocculation if necessary.
A(impurity) + B(reagent) = C (precipitate) + D(by product)
It is clearly essential that any byproduct of the reaction does not itself have undesirable properties in relation to the eventual use of the water or wastewater. It is also important to remember that chemical precipitation processes produce sludge's containing the impurities and that the cost of handling and disposing of these sludge's in a safe manner can be significant. (THY Tebbutt, 1990)
Disinfection refers to the selective destroy of disease causing organism .all the organisms are not destroyed of during the process; this differentiates disinfection from sterilization, which is the destruction of all organisms. In the field of waste water treatment, there are three categories of human enteric organisms of the greatest consequence in producing disease are viruses, bacteria, and amoebic cysts.
Disinfection is widely used to wastewater sewage treatment plant; there are well -established links between the contamination of drinking water with facial matter and the incidence of such water related diseases as cholera, typhoid and many gastrointestinal infections. Thus the removal of the pathogenic microorganisms from water supplies is a very valuable measure for the improvement of public health. Disinfection means the destruction of pathogenic microorganisms and does not necessarily mean that the water is sterile, since a small number of harmless microorganisms are usually present in tap water and poses no hazard.
For most disinfection the rate of kill is given by
dN/dt = -KN
where k = rate constant
N = number of living microorganisms
The rate constant varies with the particular disinfectant, its concentration, the organism being killed,PH,Temperature,and other environmental factors. (THY Tebbutt, 1990)
Sewage Treatment plant is widely used to Biological unit processes ,this is processes is remove the microorganism of the water, In this Treatment methods in which the removal of contaminants is bring about by biological activity are known as a biological unit processes. Biological treatment is used primary to remove the biodegradable organic substances matter (means colloidal or dissolved )in wastewater.Basically,these substances matter are converted into the gases that can be escaped to the atmosphere and into the biological cell tissue unit that can be removed by settling. At the same time this treatment is also used to remove the nutrients (means nitrogen and phosphorous) in wastewater. (George Tchobanoglous, FranKlin L.Burton, 1991,1979,1972)
The components of the wastewater flows that make up the wastewater flow from a community depend on the type of collection system used and may include the following:
There are four types of wastewater flows available in the wastewater treatment.
1. Domestic (is also called sanitary) wastewater. This is kind of wastewater discharged from residences and from commercial,instutional , and house hold sewage toilet waste water, bath, sinks ,and canteen wastewater and similar facilities.
2. Industrial wastewater .this kind of wastewater in which industrial wastes predominate.
3. Infiltration/inflow .water that enters the sewer system through the indirect and direct means. The Infiltration is extraneous water enters that the sewer system through the leaking joints.
4. Storm water. Runoff resulting from rainfall and snowmelt. This kind of components of wastewater flows essentially used in the sewage treatment plant.
There are four different types of wastewater processing in available in sewage treatment plant. Primary treatment referred to physical unit operations. Secondary treatment referred to chemical and Biological unit process, and also Advanced or tertiary referred to combinations of all four other processing.
Â· Preliminary wastewater treatment:
Preliminary wastewater treatment is defined as the removal of wastewater constituents that may causes to maintenance of the operational problems with the treatment of the operations. Examples of preliminary operations are screening and commutation for the removal of debris (J.Staudenmann, A. Schonborn, C. Etnier, 1996).primary wastewater treatment:
In primary wastewater treatment, a portion of the suspended solids and organic material is removing from the waste water. This removal is usually accomplished with physical operations such as screening and sedimentation. The effluent from primary treatment will ordinarily contain considerable organic matter and will have relatively high BOD.treatment plants using only primary treatment will be phased out in the future as implementation of the EPA secondary treatment requirements is completed. Rare instances (for those communities having a secondary treatment waiver)will primary treatment be used as the sole method of treatment .the principal function of primary treatment will continue to be as a precursor to secondary treatment .
* Conventional secondary wastewater treatment:
The secondary treatment is directed principally toward the removal of bio degradable organics and suspended. Disinfection is included frequently in the definition of conventional secondary treatment is defined as the combination of processes customarily used for the removal of these constituents and includes biological treatment by activated sludge fixed film reactors, or lagoon systems and sedimentation.
Â· Advanced wastewater treatment/wastewater reclamation:
Advanced wastewater treatment is defined as the level of treatment required beyond conventional secondary treatment to removing constituents of concern including toxic, nutrients, compounds, and larger amounts of organic material and suspended solids .In addition to the nutrient removal processes, unit operations or processes frequently employed in advanced wastewater treatment are chemical coagulation, flocculation, and sedimentation followed by filtration and multi grade filter and also activated carbon filter. (George Tchobanoglous, FranKlin L.Burton, 1991,1979,1972).
A Rotating biological contactor (RBC) is constructed of bundles of plastic packing attached radically to a shaft, forming a cylinder of media .the shaft is placed contour bottomed tank so that the media are submerged approximately 40 percent. the contactor surfaces are spaced so that during submergence in wastewater can enter the voids in the packing .when rotated out of the tank ,the liquid trickles out of the voids in the packing. when rotated out of the tank the liquid trickles out of the voids between surfaces and is replaced by air. A fixed film biological growth, similar to that on a trickling filter packing, adheres to the media surfaces. Alternating exposure to organics in the wastewater and oxygen in the air during rotation distributor. Excess the biomass sloughs from the media and is carried out in the processes effluent for gravity separation.
A treatment system consists of primary sedimentation preceding and final sedimentation following the rotating biological contactors. Since the recirculation through RBC units is not normally practiced, only sufficient underflow from the final clarifier is returned to allow removal of excess of the biological solids in primary sedimentation and waste sludge similar to the character to the from trickling filter plant ,in withdrawn from the primary clarifiers disposal of waste. In large type of plants, a common shaft is placed over a contoured tank with the wastewater flow parallel to the shaft. A series of four stages are normally installed in the treatment of domestic wastewater for BOD reduction. additional stages may be added to initiate nitrification .Each stage acts as a completely mixed chamber and the movement of the wastewater through the series of tanks simulates plug flow. Biological solids washed off of the media are transported hydraulically under the baffles to be carried out with the effluent.RBC units are protected by installation either in a building with adequate ventilation or under separate plastic covers lined with insulation.
The efficiency of BOD removal of in the processing domestic wastewater is based on empirical data from operating RBC plants. the Mathematical equations also have been developed ,but their prediction of the performance is not consistently reliable. the typically recommendations for secondary treatment of domestic wastewater to produce an effluent of less than 30 mg/l of BOD and also 30mg/l of suspended solids. (Mark J.Hammer Mark J.Hammer,Jr, 1996)
TECHNICAL DETAILS OF RBC:
DESCRIPTION MOC / MAK
1. Polymer sheet die 2m x 2 thk - special polymer from Germany
2. RBC Trough - poly propylene /FRP
3. RBC Support - MS Resin Coated
4. Geared Motor (0.75HP) - FLENDER
5. Input Coupling - Love Joy
6. Drive Support - Mild Steel
7. Bush - Nylon
8. Shaft - SS304
TANK SCHEDULE OF RBC :
The following tanks used in sewage treatment plant based Rotating Biological contactor Processes.
1. Bar screen
2. Collection Tank
3. PIT 1,2,3
4. Flow divider
5. Sludge drying bed
6. Semi Treated water tank
7. Multi grade sand filter
8. Activated carbon filter
9. Treated water tank
The following equipments used in sewage treatment plant based Rotating Biological contactor processes.
DESCRIPTION MODEL/HP QTY
RBC 0.75 hp 1
Submersible Pump 1 Hp 2
Submersible Pump (Lamella) 1 Hp 1
Filter feed submersible pump 3 Hp 2
Raw sewage characteristics:
Domestic waste water:
The volume of a wastewater from a community varies from 50 to 250 gal capital per day depending on the sewer system uses. A common values for domestic wastewater flow is 120 gpcd means 450 liter person per day use, which assumes that the residential waste water have modern water using appliances, such as automatic washing machines. the organic substances matter contributed per person per day in domestic wastewater is approximately 0.24 lb to 110gram of suspended solids and 0.20lb and 90 gram of BOD in communities where a substantial portion of the household kitchen wastes is designed is discharged to the sewer system through garbage grinders. In selection of data for design, the quantity of and organic strength of wastewater should be based on actual measurements taken through the year to account for variations resulting from seasonal climatic changes and other factors. the average values during the peak month may be used for design ,excluding un usual infiltration and inflow, the average daily sanitary wastewater flow during the maximum month of the year is commonly 20 to 30 percent greater than the average annual daily flow, excluding seasonal industrial wastes, the average daily BOD load from sanitary wastewater during the maximum month is greater than the annual average by 30 percent or more in small plants less than 0.5 mgd and less than 20 percent in large plants greater than 50 mgd. (Mark J.Hammer Mark J.Hammer,Jr, 1996).
In municipal wastewater flow in sanitary sewers is a composite of domestic and industrial wastewaters, there are two flows infiltration and inflow, and intercepted flow from combined sewers. Collector sewers must have hydraulic capacities to handle maximum hourly flow including domestic and infiltration, the new sewer systems are usually designed on the basics of an average daily per capital flow of 100 gal of 400 litres. However, pipes must be sized to carry peak flows that are many times assumed to be 400 gpcd and 1500 liter person used. waste strength is greatest during the workday when household and industrial activities are contributing a larger amount of organic matter, and it is reduced during the night when entering flow is less contaminated and slow velocities in pipes permit the settling solids. if both flow and BOD concentration variation are known, as the knowledge of influent hydraulic and BOD loadings are essential in evaluating the operation of a treatment plant. (Mark J.Hammer Mark J.Hammer,Jr, 1996).
Graph: Variation in concentration of BOD in the waste water and resulting BOD loading pattern. (Mark J.Hammer Mark J.Hammer,Jr, 1996)
Graph: Waste water flow and strength variations for typical medium sized city.
(Mark J.Hammer Mark J.Hammer,Jr, 1996).
From the flow divider the sewage will enter the RBC. In the RBC the BOD / COD digestion will take place. The disks which will have the fine surface will allow the bacteria to grow in its surface. The surface area will decide the Colonization of bacterial mass.
Rotating Biological Contractors (RBCs)
The RBC process consists of a series of closely spaced discs (2m) in diameter) mounted on a horizontal shaft and rotated, while about one - half of their surface area is immersed in wastewater. The discs are typically constructed of lightweight plastic. The speed of rotation of the discs is adjustable.
When the process is placed on operation , the microbes in the wastewater begin to adhere to the rotating surface and grow there until the entire surface area of the discs is covered with a 1- to 3 mm layer of biological slime. As the discs rotate, they carry a film of wastewater into the air; this wastewater trickles down the surface the discs, absorbing oxygen. As the discs complete their rotation, the film of water mixes with the reservoir of wastewater, adding to the oxygen in the reservoir and mixing the treated and partially treated wastewater. As the attached microbes pass through the reservoir, they absorb other organics for breakdown. The excess growth of microbes is sheared from the disc as they move through the reservoir. These dislodged organisms are kept in suspension by the moving discs. Thus, the discs serve several purpose: (George Tchobanoglous and Franklin L. Burton, 1991)
1. They provide media for the buildup of attached growth.
2. They bring the growth into contract with the wastewater.
3. They aerate the wastewater and the suspended microbial growth in the reservoir.
4. The attached growths are similar in concept to a trickling filter, except the microbes are passed through the wastewater rather than wastewater passing over the microbes. Some of the advantages of both the trickling filter and activated sludge processes are realized.
As the treated wastewater flows from the reservoir below the discs, it carries the suspended growths out to a downstream settling basin for removal. The process can achieve secondary effluent or better. By placing several sets of discs in series, it is possible to achieve even higher degrees of treatment, including biological conversation of ammonia to nitrates (George Tchobanoglous, FranKlin L.Burton, 1991,1979,1972).
We have provided in total 80 nos of disks . The disks are 2mtr diameter 2 mm thick.
The total surface Area : 502 M2
The disk are rotating in a slow rpm thereby allow the colony of bacteria to expose in the atmosphere and sewage water alternately. This will allow enough oxygen for the mass to grow and also will digest the BOD / COD levels in the sewage water. This 'Fixed film' growth in the disk, unlike conventional STP will be denser and due to that the space will be small.
RBC Design Calculation of water consumption:
Total Raw water BOD5 = 250 mg / ltr x 50 KLD
= 12500 g / day.
Primary Treatment = 15 % Reduction
i.e 2437g/day reduction in primary and available BOD is 13813 g/day.
Available BOD = 10625 g / day.
BOD loading : 30 g/m2/day
i.e since being a attached growth system the standard for BOD digestion in the disk is 30 gram per day per m2 of available surface area of the disk.
Disk Surface Required = BOD5 g / day : 30 g / (M2 x d)
= 10625 / 30
Surface Area Required = 354 M2
Diameter of one disk d : 2.0
Area of one disk : 2 x P (2.0) 2: 6.28 m2.(Taking consideration of both side of the disk
No of disk selected: 80 any
Total Surface Available : 502 m2.
Our requirement of 354 m2 of surface area meets out with available surface area of 502 m2 , which 40% more than the requirement.
Surface area available is much more than required. This will take care of a maximum flow of 70KLD where as the actual flow will be only 17 KLD plant.
Length of trough (each chamber) : 1990 mm
Diameter of trough : 2200 mm
30%onlyfilled with water
Volume Pd2 x L x 0.3= 2.27 m3.
Specific Retention time required : 0.33 hrs.
Specific retention time for the trough in the RBC is 0.33 hrs for the digestion of 30 g/m2/day BOD5 in a uniform loading.
Assumption: Film growth around 1.5 - 2 mm thickness
Retention time available
Flow : 50 KLD
Flow in m3/hr : 2 m3 / hr
Retention time = Volume of Trough
Flow in m3 / hr = 2.27 m3
2 = 1.135 hours
The retention time actually required is 0.33 hrs where as available retention time for the uniform flow of 2 m3/hr is 1.135 hours.
After the RBC the sewage water will pass through Lamella separator where the suspended matter will settle down. The settled biomass at the Lamella underflow will be sent to the sludge drying bed periodically. There is no need for recycling of the sludge as like in the conventional aeration system. The overflow from the Lamella clarifier will be the semi treated clarified water.
Retention time required : 0.4 - 0.6 m3 / hr /m2
Size of LMS = 1.275 x 1.42 x 2.11(Total height) with 673 mm conical height
Volume = 3.2 m3
Retention time available = -------- = 1.6 hrs
2 m3 / hr
Whereas the required levels are 0.4 - 0.6 m / hr
Treated effluent characteristics:
Advantages of RBC:
Â· RBC s are capable of handling a wide range of flows.
Â· Operating costs are low because little skill is required.
Â· Short retention time.
Â· Low power required.
Â· Low Sludge production.
Â· Excellent process control.
Â· Shaft bearings and mechanical drive units require frequent maintenance.
A pump is a device of essential used to move fluids, such as gases liquids. A Pump displaces a volume by physically or mechanically action and operation. one common function of pump is the create a pressure. Pumps alone do not create a pressure, only displace fluid, and causing a flow .the pumps resistance to flow causes pressure. it is a pumps falling into five major groups, in which a displacement,velocity,direct lift, gravity and buoyancy pumps. these types of pumps describe the method for moving fluid.
Engineers first preferred pumps to deliver a liquid or gas to specific place at a essential rate. Liquids and gases are known as a fluids. A pump is normally used to change the elevation, velocity or pressure of a fluid. In naturally, a fluid will flow naturally from the high place to a low place like a water fall or from the high pressure. to a low pressure from the inside a balloon to the outside air. its velocity is many times function of geometry and the conditions around it. when a fluid is required to from a source like a pond, at a higher pressure than a source, or at a higher rate and expert engineers will only consider a pump to accomplish the task.
This lessons will be broken into the five basic sections and basic terms also included, fluid statics and flow rates and the Bernouli equation, and a form of the energy equation for pumps .As it progresses, we will move from the basic definitions and terms to find out the power of an idealized pump. Some of the terms we need to start with are gravity or the gravitational constant, density and also pressure. (mechanicalpumps.com).
The sewage treatment plant is mostly used to submersible pump because this type of pump is very high efficiency at same time efficient of the processes.
The sewage submersible pump is suitable for effluent tranfer in domestic waste water treatment plant,and also industrial applications,where suspended solids need to be reduced in size and pumped over the short to medium distance,this pump shaft is 304 stainless steel fitted with a double mechanical seal in an oil chamber.this pump with 10 meters of heavy duty processes.submersible pump costructed in cast iron and 304 stainless steel. (http://www.southernpumpservices.co.uk/submersable_water_pump_history.htm
Submersible pump is mostly used in sewage treatment plant which is used inside the water, this type of sewage pumps with power up to 70kw(95 HP).this type of pump mounted in cast iron and stainless steel construction. The full range includes single and multi channel and also self cleaning for managing solids with fibers and mounted in vortex impeller, grinding version also available in submersible pump. There are four model of submersible pumps used to DLS, DLV, DLC, DLG Sewage treatment plant.
Submersible pumps originally used in Europe, submersiblewastewater, foulwater, And Sewage pumps first were seen in the United States in the mid 1950s.submersible pumps are the dominant feature in the pumping station market. A submersible pump includes not only the pump motor unit, but sophisticated to both electrical and mechanical controls, piping and wet well with access frame and cover,tooThe submersible solids handling sewage pump operates under water and is flood proof. It is basically designed for single or dual, wet (http://www.southernpumpservices.co.uk/submersable_water_pump_history.htm
The pump is efficient, and very quiet in operation, safe to install and performs long and reliability, the submersible wastewater pump is used primary for wet pit sewage pump station and for industrial sump or processes effluent applications, a common used for small pumps is to move effluent from the tank.
Large and small units are used in a different of ways in the home, farm hotel and school, marine, commercial building, industrial plant and municipal or domestic sewage and storm water pump processes or systems. Submersible pumps have been proven over the last half of a century, and disproving those who originally questioned how electric motor powered pump was could run under water. These pumps originally developed in Europe countries, and at same time now are used daily throughout the world to pump clear water, raw water and waste water.
The submersible pump used to wastewater, foul water, and surface water and sewage pump became popular in the early 1960s,when a guide rail system was developed to lift the pump out of the pit for the repair. This ended the dirty and sometimes difficult task of sending people into the sewage or wet bit. Growth of the submersible for wastewater pumping since has been change and improvement, as an increasing number of specifies and users learned of its advantages. two types of classes of submersible exist, the smaller units commonly called sewage ejectors, are used in house and light commercial applications, they will normally handle up to 55mm spherical solids and ranges from .75kilowatt to 2.2kilowatt.
Larger submersible pump handle 65mm and larger solids and have a minimum of 80mm discharge. They are used in municipal wastewater and industrial applications for pumping sewage and all types of industrial wastewater.
Model = DLS, DLV, DLC, DLG
Delivery = up to 1.500,00 m3/hour
Head = up to 82, 0 m
Power supply = both 1 and 3 50HZ.
Power = Ranges from 0.95kw up to 70,00kw
Temperature of pumped liquid = 40 degree Celsius.
1. Residential waste water
2. Commercial waste water
3. Light industry waste water
4. Municipality waste water (Refhttp://www.lowara.co.uk/products/product.)
Submersible pump features:
The submersible waste water pumps are vertical, direct coupled, extra heavy duty units, which have operate under the water and have solids handling, and non clog capability. while single pumps many times are installed ,most application are require two pumps this is called duplex to ensure two and to ensure continued processes of operation, if one pump fails to minimize wear on one pump and equalize it between two and to provide extra capacity in times of extraordinary loads.
A submersible pumping system consists of the motor pump unit together with automatic electrical controls. Controls can be simple or complex, depending on the application. The latter may consists of an entire factory packaged station enclosed in a steel or tank of fiberglass tank and ready for the installation and pipe electrical hook up. Submersible are being specified increasingly in applications where self priming, dry pit, straight centrifugal, vertical extended shaft and pneumatic rejecter pumps once dominated.
Submersible pumps is depending on the impeller design, a 100mm discharge pump normally will handle spherical solids of 80mm.each manufactures literature specifies the maximum of solids size, which can be handled by a particular pump. Normal discharge sizes for larger submersible is ranges from 80mm to 600mm and larger. This type of pump selected should be sized to the application. Submersible pump motors also can be sized to the application.
The normally submersible pumps are available in 950, 1450 and 2900 rotation per minute, on 50 cycle power .kilo watt ratings ranges up to 200kilowatt or larger. The variable speed unit also is available with the use of variable frequency and voltage power supplies. Again depending on the application of the motors operating on, 230 volts and 415 volts are available and may be single or three phases. Single phase units usually are limited to 2.2 kilowatt.thus, submersible can be tailored to job essentials. Like any pumps, especially submersibles also can be tailored to the capacity needed of the particular installation. A specified can be ask for a high dynamic head, or can accept a lower head and obtain a higher L/S or can get both the higher head and a higher flow rate by increasing the kilowatt rating. Typically heads ranges from 2.5 meters to 95 meters. Flow rates ranges from 21/s to be 2001/s, and larger submersible pumps produce 6000 1/s 0r more. The pump motor unit can be tailored to installation requirements. Many larger submersible pumps can be used in conjunction with a variable speed drive to further fit the performance to theapplication..(http://www.southernpumpservices.co.uk/submersable_water_pump_history.htm
Pumping system components:
To design a cost effective pumping system it is not sufficient to just consider only the basic head and flow needed of the pump, as a number of other factors need to be taken into consideration, Source of effluent within the inlet gravity system, and the nature of the liquid to be handled. The pump hydraulic design and the best suited materials of construction. Pump size and effective volume of the pump sump and consideration of liquid depth and its effect on pump performance. The internal shaping of the pump sump, for wet well applications and to prevent sedimentation wastewater processes. The correct spacing and positioning of pumps within the wet well applications.
The design of the pump inlet pipe work for dry well applications. The sizing and design of the pump station discharge pipe work under all operating conditions. The pumping system of components sizing and design of the pump main consideration. The effects of variable liquid levels at the final discharge of point on the pump performance curve. Source of power supply, and current limitations and motor starting method.
TECHNICAL SPECIFICATION & ASSUMPTION:
Model = DOC
Delivery = up to 14 m3/hour
Head = up to 11,0 m
Power supply = both 1 and 3 50HZ.
Power = Ranges from 0.25kw up to 0.55kw
Pump total head = 11 meter
To pump total head converted into feet 1 meter = 3.280 feet
So submersible pump total head 11 meter = 36.08 feet (calculateme.com)
Submersible pump delivery Q = 14m3/hour
Submersible pump delivery convert into gallons per minute,1 m3/hour = 4.4028gallons/min.
Total submersible pump delivery Q = 14 m3 /hour = 61.640 gallons/min (unitconversion.org)
Rotating Biological contactor based sewage treatment plant water influent is 60 kilo liter per day, Assumption of water influent is =60 KLD
To kilo liter per day convert into gallons per hour
Total delivery of influent Q = 60 549.92 gallons per hour
To gallons per hour convert into gallons per minute Q = 549.92 gallons/hour
Q = 9.165 gpm
To calculate the pump water horse power,
Water horse power formula (Whp) is =
The following data is given delivery Q = 9.165 gpm
Total head = 36.08feet
Water horse power formula(Whp) is, =
Pump water horse power is (Whp) = 0.08 Hp.
Then to calculate the pump Brake Horse power,
Submersible pump power ranges from 0.25kw to 0.55 kw
Actually power required to run the water is =0.55kw
To find out pump Brake Horse Power,(BHP) =
Submersible pump efficiency is assumed at constant =50 to 85% efficiency,
To Brake Horse power (BHP) = ( take average efficiency of the motor)
Pump Brake Horse power (Bhp) = 0.12 hp.
Then to find out the pump motor horse power (Mhp) =
BHP = 0.12 hp,
Motor efficiency =85% or 0.85
Pump Motor horse power(Mhp) =
Motor horse power(Mhp) is = 0.145 Hp
Kilowatts of energy consumed per day
How much amount of energy consumed in submersible pump,
Kilowatts hours day formula = hp x 0.746 kw/hp x 12 hr/day
Actual working of pump 12 hrs/day = 0.24 watts x 12 hrs/day
Pump energy consumed per day = 2.88 kw hour/day
Actual pump power ranges from 0.25kw to 0.55kw
Covert into watts from the power,actual power used 0.25 x 2 = 0.50 watts.
Power required to run the system part = 2.88 kw hour/day
Actual power used = 0.50 watts X 12 hour/day
= 6 kwh/day.
To finout power loss = power required to run the system - Actual power used in the plant = 6 kwh/day - 2.88 kwh/day
= 3.12 kwh/day
Power loss = 0.26 kilowatts
The major drawback of RBC is the breakdown of shaft bearing and mechanical drive units. From the calculations of submersible pump, 0.25 KW to 0.55 KW range of pump power, 0.20 watts of power is lost. When compared to other pumps such as centrifugal and self priming pumps ,there is minimum power loss in submersible pumps because the location of the pump.( Submerged in water).
The sewage treatment plant has been successfully analyzed. The 2D analysis of Rotating Biological Contactor has been done. The analysis of water consumption and power consumption has been done.
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* George Tchobanoglous, FranKlin L.Burton. (1991,1979,1972). WasteWater Engineering Treatment Disposal Resue. In WasteWater Engineering Treatment Disposal Resue. (Vol. III). Us: Metcalf & Eddy.
* J.Staudenmann, A. Schonborn, C. Etnier. (1996). Recycling the Resource, Ecological Engineering for Wastewater \treatment (Vols. 5-6). Transtec Publication, UK.
* Mark J.Hammer Mark J.Hammer,Jr. (1996). water and wastewater technology. In water and wastewater technology. prentice-hall,inc.
* mechanicalpumps.com. (n.d.). www.mechanicalpumps.com. Retrieved from http://www.mechanicalpumps.com
* Norcross.K.L. (1992). Sequencing Batch Reactors-An Overview,Water Science and Technology.
* THY Tebbutt. BASIC water and wastewater treatment.
* THY Tebbutt. (1990). Basic water and wastewater treatment. Butterworth &co.
* unitconversion.org. (n.d.). unitconversion.org. Retrieved from http://www.unitconversion.org/flow/cubic-meters-per-hour-to-gallons-us--per-minute-conversion.html