Biomethanation
in india, biomass gasification in India, bio gas, trends, costs of biomethanation and biomass gassifiers, types, business challenges, opportunities
Biomethanation involves the
biodegradation of organic wastes under strict anaerobic conditions to yield
methane-rich biogas.
Biomethanation of aqueous wastes
involves hydrolysis, acidogenesis, acetogenesis and methanogenesis reactions,
which generates a mixture of methane, carbon dioxide and other gases.
Biomethanation can be carried out in
a single step or two steps.
In the process of hydrolysis,
anaerobic bacteria breakdown complex organic molecules such as protein,
cellulose, lignin and lipids into soluble monomer molecules such as amino
acids, glucose, fatty acids and glycerol. Hydrolysis phase is relatively slow.
Acidogenic bacteria convert sugar,
amino acids and fatty acids to organic acids, alcohols and ketones, acetate, Co2
and H2. The products formed vary with type of bacteria as well as
with the temperature, PH etc.
Acetogenic bacteria convert fatty
acids and alcohols into acetate, hydrogen and carbon dioxide. Acetogenic
bacteria require low hydrogen for fatty acids conversion.
Methanogenesis is the formation of
methane by microbes known as methanogens. Methanogenesis in microbes is a form
of anaerobic respiration. Methanogens do not use oxygen to respire;
in fact, oxygen inhibits the growth of methanogens. The terminal electron
acceptor in methanogenesis is carbon.
The two best described pathways
involve the use of carbon dioxide and acetic acid as
terminal electron acceptors:
CO2 + 4 H2 →
CH4 + 2H2O
CH3COOH → CH4 +
CO2
The process of small-scale
Biomethanation includes feedstock colleting, pretreatment, fermentation,
treatment and purifying, storage and transportation.
Batch fermentation and
semi-continuous fermentation are usual technologies for small-scale
biomethanation. In batch fermentation technology, all the feedstock is added at
the first. The biomethane generates fast at the beginning and then decreases.
In semi-continuous fermentation technology, ¼ - ½ feedstock was added at the
first. When the biomethane generation slows down, more feedstock is added to
make the biomethane generation work in order.
Large – scale anaerobic digestion
systems:
Pre-treatment process:
The biomass waste is conditioned in
a pre-treatment process such as removal of foreign matters not suitable for
anaerobic digestion, pulverization, dilution by water, thickening, and/or
acid/alkali treatment. Some biomass wastes such as garbage, which is a mixture
of various organic and inorganic matters, and, thus, is not always consistent
in its composition and properties, are subjected to mechanical and/or magnetic
separation in order to get rid of indigestible materials such as metals and
plastics. The separated biomass waste is pulverized and added with dilution
water to prepare waste slurry for the next unit process.
Slurry storage tank:
Prepared slurry is temporarily
stored in a slurry storage tank for leveling diary fluctuations in both quality
and quantity. If the ambient temperature is suitable, microbial activities of
acidogens in the storage tank may increase. If this occurs, accumulation of
organic acids in the slurry can cause a decrease in pH to as low as around 4.
The slurry storage tank must be designed to resist corrosion due to such low pH
conditions.
Methane fermenter:
Three major functional microbial
groups are active in the methane fermenter. These three functions that take
place sequentially are; hydrolysis, acidogenesis and methanogenesis. The final
products of the reactions are methane and carbon dioxide. The hydrolysis
reaction is often the rate-limiting pathway of an anaerobic digestion process
on not-readily biodegradable or recalcitrant biomass such as sewage sludge and
ligneous biomass, whereas the methanogenesis is likely to be the rate-limiting
pathway on readily biodegradable biomass such as garbage and starchy waste
water. In order to establish an efficient anaerobic digestion system, it is
important to consider the rate-limiting pathway and to select the most suitable
reactor design for the properties of anticipated biomass waste.
Fermentation waste water treatment:
Fermentation waste water discharged
from the anaerobic digester usually contains high concentrations of organic
matters, nitrogen compounds and phosphorous compounds. The fermentation waste
water should be treated to reduce the concentration of these pollutants to meet
the standards for final discharge to a receiving body of water or sewer system.
The most typical fermentation waste water treatment system is the activated
sludge process with tertiary treatment.
Biogas utilization:
Since most of the biomass waste
contain proteins and sulfate salts, the biogas contain certain concentrations
of hydrogen sulfide and ammonia, The biogas produced from sewage sludge, which
sometimes contains a considerable amount of silicones, may contain siloxanes as
well. Since these impurities can possibly cause damage to biogas utilization
facilities such as a gas engine, gas boiler, gas turbine and fuel cell, and/or
cause secondary air pollution, a biogas utilization unit process is often
equipped with a desulfurization device and/or siloxane remover prior to the gas
holding tank.
Advantages of Biomethanation:
- Production of thermal and electrical energy from waste or fermentable sub-products\
- Reduction in greenhouse gas emissions: Co2 and CH4
- Economic solution for the treatment of organic waste
- Agricultural diversification and recycling
An example of the economic viability
of Bio-methanation plants
Project Case: 2 MW Biogas to Power
plant
Total Investment: Rs.260 Million
(Rs.130 Million/MW)
Capital subsidy (CFA): Rs.15
Million/MW (for mixed waste)
Plant Load Factor: 80% - 82%
Present power tariff band: Rs. 4.24
– 4.7/kWhr
Approx feedstock Reqmt: 11 Mt/MWhr @
45% DS Content
Average Min Feedstock price:
Rs.600/MT (landed at Site)
Price for Organic Compost: Rs.600/MT
(current market prices)
Carbon Credits Revenues: 10000 –
20000 Credits/Annum
Overview of financial viability with
CER Revenue:
Financial Indicators
|
Unit
|
Tariff at Rs.4.5/kWhr
|
Tariff at Rs.5.75/kWhr
|
|
|
|
|
Equity
|
%
|
30%
|
30%
|
Debt
|
%
|
70%
|
70%
|
|
|
|
|
Cost of Debt (min)
|
%
|
11%
|
11%
|
Equity IRR (pre tax)
|
%
|
9.0%
|
19.5%
|
Project IRR
|
%
|
10.7%
|
18.0%
|
Payback time
|
Years
|
9.2
|
5.45
|
Other Assumptions:
CFA: Rs.15 Million / MW
Sale price of Compost: Rs.1200/MT
CER Revenue: € 10 /CER
Overview of financial viability with
CER Revenue:
Financial Indicators
|
Unit
|
Tariff at Rs.4.5/kWhr
|
Tariff at Rs.5.75/kWhr
|
|
|
|
|
Equity
|
%
|
30%
|
30%
|
Debt
|
%
|
70%
|
70%
|
|
|
|
|
Cost of Debt (min)
|
%
|
11%
|
11%
|
Equity IRR (pre tax)
|
%
|
3.5%
|
14.2%
|
Project IRR
|
%
|
5.7%
|
14.3%
|
Payback time
|
Years
|
12.3
|
6.8
|
Other Assumptions:
CFA: Rs.15 Million / MW
Sale price of Compost: Rs.1200/MT
CER Revenue: € 10 /CER
Biomethanation plants in India:
Biomethanation for Treatment of
Slaughterhouse Waste at Medak, Andhra Pradesh (2 units of plants):
The first phase biomethanation plant
for treatment of abattoir waste has been completed at M/s Al kabeer Exports
Ltd., Medak, Andhra Pradesh, having an installed capacity of slaughtering and
processing 500 - 600 buffaloes and 1500 - 2000 sheep / day. The methane
digester is based on UASB (Up-flow Anaerobic Sludge Blanket) technology and
results in COD reduction of 75 to 80% and BOD reduction of 85 to 90%, besides
producing about 3500 to 4500 cum/day of biogas having a methane content of
about 65%. Adoption of the biomethanation technology has resulted in a saving
of Rs.30 lakhs per annum on account of expenditure on chemicals besides an
additional annual saving of Rs.30 lakhs on account of saving of furnace
oil. The successful adoption of this innovative technology has
encouraged M/s Al-kabeer to set up one more biogas plant for the treatment of
solid wastes, which is based on a state-of-the-art technology obtained from
Austria. These biomethanation installations have shown the way to solve
the problem of waste treatment and disposal in environmentally benign manner,
which also appears to be financially profitable.
Biomethanation Plant for Mixed
Wastes at Vijayawada:
A demonstration plant based on
biomethanation of 20 tonnes per day mixed wastes (i.e. 16 tonnes of vegetable
market waste and 4 tonnes of slaughterhouse waste and sewage from the sewage
treatment plant for dilution) for generation of power to Vijayawada Municipal
Corporation (VMC), Vijayawada has been commissioned in February 2004. The generation
of biogas is about 1600 cum; besides 5 tonnes of organic manure per
day. The biogas so produced is being used in a 145 kW imported
biogas engine for generation of electricity. The electricity
generated is fed into the state electricity grid.
Power generation through
Biomethanation of Animal Waste at Ludhiana:
Haebowal Dairy Complex in Ludhiana,
spread over an area of 50 acres, has 1490 dairies with an animal population of
1,50,000 and generate about 2475 tonnes of animal droppings. The project
utilize about 235 tonnes of waste per day to generate about 0.965 MW electrical
energy. The surplus energy after meeting the in house power
requirement is fed to the state grid. Besides, the electrical
energy, the project also produced stabilized organic manure (about 7 tonne of
70% solids and 40 tonnes of 50% solids) per day. The plant was commissioned in
June 2004, and since then it is working satisfactorily.
Biomethanation Plant for Vegetable
Market Wastes at Chennai:
A demonstration biomethanation plant
for treatment of 30 tonnes per day Vegetable Market Wastes for Generation
of Power at Koyembedu Market Complex (KMC), Chennai was approved in March
2003. The expected generation of biogas is about 2500 cum., besides 9-10
tonnes of organic manure having moisture content of 25-30% per day. The biogas
produced is to be utilized in a 230 kW imported gas engine having in built
co-generation unit for generation of electricity and thermal energy. The
total cost of the sub-project is Rs. 352 lakh plus USD 320000 with NBB/ MNRE
share of Rs. 264 lakh and USD 2,40,000. The plant is currently under
commissioning.
Biomethanation technology
providers/suppliers in India:
ION EXHANGE WATERLEAU LTD.
ION HOUSE,PLOT NO 2,
SECTOR 18,
VASHI
NAVI MUMBAI 400705
TEL :0091-22-39132298
0091-22-39890909
Website
:www.ionexchangewaterleau.com
www. ionindia.com
Contact : Ajay Popat -CEO
EMAIL
:ajay.popat@ionexchange.co.in
M/s ENKEM Engineers Pvt.
Ltd
824, Poonamalle High Road,
Kilpauk (Near KMC),
Chennai - 600010
Tel: 044-26411362/26428992
Fax: 044-26411788
Email: enkem2000@vsnl.net
M/s Mailhem Engineers Pvt. Ltd.,
14, Vishrambag Society,
Senapati Bapat Road,
Pune - 411 016.
Tel: 020-24002285
Fax: 020-25659857
Email: info@mailhem.com
M/s REVA Enviro Systems Pvt. Ltd.,
3, Suyog Nagar, Ring Road
Nagpur - 440 015
Tel.: 0712-2743123, 2743124
Fax: 0712-2743120
M/s Linde Process Technologies India
Ltd.
38, Nutan Bharat Society, Alkapuri
Vadodara - 390 007
Tel: 0265-2336319, 2336196
Fax: 0265-2335213/2313629
M/s Hydroair Tectonoics Pvt. Ltd.,
401, “Devavrata”, Sector-17,
Vashi, Navi Mumbai-400 705
Tel.: 022-27892813/68/95
Fax: 022-27893892
M/s Chemtrols Engineering Ltd.,
Amar Hill, Saki Vihar Road,
Powai, Mumbai-400 072;
Tel: 022 –28575089/ 28570557
Fax: 022-28571913
Email: jaypee@chemtrols.org
M/s Degrimont India Ltd.
Water and the Environment
D-43, South Extension - II
New Delhi - 110 049
Tel.: 011-26481191, 26481192
Fax: 011-26228782
M/s Global Environmental Engg. Ltd.
1233/C, K. G. Mansion
Opp. Hotel Kohinoor Executive
Apte. Road, Pune - 411 004
Tel.: 0212-2327876, 2328007
Fax: 0212-2328441
M/s UEM India Limited,
D-19, Kalkaji,
New Delhi-110 019
Tel.: 011-26447825/ 26421634
Fax: 011-26239801
Email: uemindia@uemgroup.com
Ion Exchange Waterleau
Ion House, Plot No.2, Sector 18
Vashi,
Navi Mumbai 400 705, India
Phone: +91-22-3989 0909
Fax: +91-22-2788 8156/2788 9839
E-mail: iewl@ionexchange.co.in
Source: http://www.eai.in/club/users/Shweta/blogs/8094
Vennar Organic Branches are in Chennai, Bangalore. We will arrange to take up the operation and will interact with the residents for source segregation and the segregated waste will be transferred to OWC room by the housekeeping staff.
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