BIOMETHANATION
PLANT BASED ON TAPIOCA PROCESSING INDUSTRY WASTEWATER AT PAPPIREDDIPATTY, TAMIL
NADU
| | : | Peppireddipatty,
Dharamapuri District, Tamil Nadu | |
| : | February,
2003 | | | : | Functioning
Satisfactory | | | : | Tamil Nadu Energy Development
Agency, Chennai | | | : | Hybrid
Upward flow sludge madia anaerobic reactor (HUSMAR) | BACKGROUND Tapioca
(Manihot Esculenta Crantz) is a crop of great economic importance, both as human
food, animal feed as well as raw material for industrial products. In India, Tapioca
is grown over an area of about 3 lakh hectares, with a production of 58 to 68
lakh tonnes of tubers. Tamil Nadu ranks second in terms of cultivation and production
of tapioca after Kerala but it stands first in respect of processing of tapioca
into sago and starch throughout the country meeting about 80 % of country's demand.
There are about one thousand sago & starch industries in small - scale sector
scattered throughout the State of which 800 units are located in and around Salem
district. About 3 cubic metre of wastewater is generated for processing one tonne
of tubers, which contains high pollution load, and has to be treated to meet pollution
norms set-up by the State Pollution Control Board. At present, there are more
than 100 units producing biogas using Tarpaulin cover over the conventional anaerobic
lagoons and utilizing the biogas produced for roasting of sago and / or for generation
of electrical energy. The wastewater of about 1200 m3 / day generated in
processing of tapioca tubers for production of starch at M/s Varalaxmi Starch
Industries Ltd., (VSIL) was therefore utilized for generation of about 0.5 MW
of electricity. The raw wastewater contains biodegradable matter such as (i) immature
/ partially matured starch; (ii) water from tapioca tubers as 55-60% of its weight
is water only; and (iii) mechanically un-extractable starch which is 1-2 % of
the total starch present in the tubers. Hybrid Upward Flow Sludge Media
Anaerobic Reactor (HUSMAR) The plant consists of two HUMSAR with 16.5
m diameter and 11.5 m height. In the central part of HUSMAR, Cross Flow Media
(CFM) is filled to a height of 4.8 m between two concrete beams. The top pf HUSMAR
tank is covered with a floating inverted tank to collect the biogas. The cross
flow media has been made of corrugated PVC sheets of 0.7 to 0.3mm thickness, 60
mm plute corrugated angle, bonded together in rectangular modules of size 1.2
m x 0.6 m x 0.6 m providing with a surface area of 102sq metre per cubic metre.
Each HUSMAR is provided with following sensors: - Flow
- pH
- Pressure
- Gas totalizors
- Temperature
The
entire plant is controlled by SCADA system. Wastewater from the equalization
tank is pumped into two anaerobic digesters operating in parallel. However, before
reaching the anaerobic digesters, the wastewater is mixed with chemicals to improve
the pH and also C: N ratio. About 85% of influent BOD is removed in these digesters.
The cross flow media provides more space for the growth of bacteria and helps
in reducing the HRT to two days and to increase the solid retention time. The
wastewater is recycled for efficient gas generation. Biogas Storage
The biogas produced as a result of stabilization of the wastewater,
leaves the digesters and is collected under a negative pressure through gas collection
header at the top of the reactor. The biogas consists of 60-65% methane and 35-40%
carbon dioxide. Effluent Treatment Plant Effluent from
the two anaerobic digesters flow by gravity into two aerobic sludge tanks which
are capable of removing > 90% of influent BOD from the effluent from the digesters.
Effluent from the sludge tanks is then taken to a secondary clarifier where
final clarification of the wastewater occurs and the final BOD concentration in
the wastewater is > 35 mg/l. PROJECT COST Total cost of
the project is Rs. 3.59 crores. TECHNOLOGY INVOLVED HUSMAR
Technology has been developed at NJIT, New York, USA. MATERIAL BALANCE
Wastewater feed: 1200m3 / day
| Parameters | Max. | Average | Min. |
- Throughput capacity, kg of COD/day
| | | |
| | | | |
| | | | |
- Biogas production cum / day
| | | |
- Electrical power generation, kWh/
day
| | | |
- Electrical power consumption in the
plant kWh / day
| | | |
- Availability of net electrical power
for other use, kWh / day
| | | |
- Consumption of chemicals in the biomethanation
plant, kg/day
| | | |
| | | | |
| | | | |
ENERGY BALANCE
- Energy generation from
the plant
| : | 500kW
| - Auxiliary power
requirement
| : | 30kW |
- Power to be used for sago production
| : | 470
kW | MANPOWER REQUIREMENT FOR PLANT BENEFITS ACHIEVED - Reduction in emission of green
house gases
- Employment generation
- Fuel Savings
- Effective
waste Management (cleanliness)
|