Introduction
Screening (Bar screen and grit chamber)
The raw sewage first be screened through a manual bar screen, where all particles with diameter below 5 mm as well as small pieces of the fibre and floating suspended matters like polythene paper, polythene bags, rags and others materials are removed. These units are used to protect downstream equipment such as pumps, pipelines, valves etc. from damage and clogging by rags and other large objects. The bar screen and grit chamber is cleaned manually by means of rakes. The screened clean effluent flows by gravity to an equalization tank.1, 2
Oil & grease chamber
The screened wastewater then gets skimmed properly to remove Oil and Grease. The removal principle based on density and viscosity of the sewage.
Equalization tank
The raw wastewater collected in the equalization tank, where it is equalized with respect to its characteristics, homogeneity, flow and uniform pollution load as well as to make bacteria acclimatized. The equalization tank is designed for hydraulic retention time of around 6 hours. Proper equalization process minimizes the shock loadings and stabilizes the pH to improve the biological oxidation reaction in the next downstream units.
Anoxic tank
Anoxic zones in wastewater are useful for nitrogen removal. Wastewater has a high nitrate and nitrite content, and the treatment process must break down those compounds to avoid causing nutrient pollution when the plant discharges its effluent back into the environment. In anoxic zones bacteria break down the nitrogen products and release nitrogen gas into the atmosphere.
MBBR tank (Secondary-treatment) 3, 4, 5
The process of Oxidation, synthesis and endogenous respiration happens in the MBBR tank or aeration tank. Eco-friendly available in the sewage facilitates the above process; hence the complex organic compound gets converted to simpler organic substance. Bacteria or bio augmenter staying in MBBR Media surface and does the job utilizing the supplied oxygen through Air blowers.
Tube settler
The oxidized sewage will be dosed with coagulants and flocculants and allowed to pass through the Tube Settler. Here the suspended solid gets settled inside the tube settler through the intact arrangements of tube settler media. A substantial amount BOD and COD are also removed in the coagulation and flocculation process.
Disinfection System
Chlorine disinfection system installed to oxidize the pathogenic bacteria from the treated sewage water and then allowed to pass through the filtration units like PSF and ACF.
Pressure Sand Filter (PSF)
From the filter feed tank, the clear water is pumped to the pressure sand filter. The filtration takes place in the downward mode. The filter is filled with a layer of graded sand media supported by a layer of graded gravel. The suspended matters from the effluent get filtered.
Sludge Treatment and handling
The sludge generated in the Sludge Holding Tank is taken to a sludge sump. The waste is then pumped to a Sludge Drying Bed. The dried cake may be disposed of to deliver in the brickfield for burning. The further waste sludge will be flow back to equalization tank for further treatment.
Sewage treatment plant existing
Project Name: Rajiv Gandhi Institute of Medical Sciences (RIMS), Kadapa A.P
Project Type: Sewage Treatment Plant.
Design Capacity: 1 MLD.
Operation Hours: 24 hrs.
Technology: Moving Bed Bioreactor (MBBR).
System Erected by: M/S. Green Enviro Polestar, Pondicherry.
Table 1
Table 2
Table 3
Results and Discussion
All the sorted water parameters were been tested by following the standard method (APHA, 1998).6, 7 The average BOD (Biochemical Oxygen Demand), COD (Chemical Oxygen Demand), TSS (Total Suspended Solids) and TKN (Total Kjeldal’s Nitrogen) removal efficiency from the existing 1 MLD Sewage treatment plant were observed to be 95%, 89%, 68.5% and 78% respectively. Hence, we could able to see very good removal efficiency of BOD, COD and TKN. A very good reduction of BOD, COD and TKN value shows that there would be a healthy bacterial growth in the MBBR Unit and proper nitrogen removal happens in the Anoxic tank. Also, a better F/M (Food to the ratio of Microorganisms) observed to be maintained in the MBBR Tank. But the TSS reduction value found to be unacceptable; hence the PSF (Pressure Sand Filter) and ACF (Activated Carbon Filter) filters need to be operated properly as per the operation manual. Both the filters needs to be backwashed at regular basis and the delta P value (Pressure difference which can be monitored through the pressure gauges) should be maintained below 0.5 Kg/Cm2. Hence, this study can be helpful for the maintenance engineers in doing proper operation of the sewage treatment plant of the RIMS Hospital.