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WASTE TO ENERGY TECHNOLOGY
REVIEWS IN INDIA
Haritha M
Assistant Professor
Dept. of Civil Engg.
1
Introduction
 Form of energy recovery
 Process of generating energy in the form of electricity or
heat from primary treatment of waste
 Waste-to-Energy means the use of modern combustion
technologies to recover energy, usually in the form of
electricity and steam
 New technologies -reduce the volume of the original waste by
90%, depending upon composition and use of outputs
2
Why we go for WTE?
 Can address two sets of environmental issues at one
stroke
 Land use and pollution from landfills
 Environmental perils of fossil fuels
 Quite expensive
 Some can be applied economically
3
Major Constraints in WTE
 Still a new concept in the country
 Lack of financial resources with Municipal
Corporations/Urban Local Bodies
 Most of the proven and commercial technologies in respect of
urban wastes are required to be imported
 Lack of conducive policy guidelines from State Governments
in respect of allotment of land, supply of garbage and power
purchase
4
Limitations of WTE
 Waste low energy density than fossil fuels-cost of energy
production increased-energy efficiency reduced
 Locating the waste processing plant near the waste resources
reduce problem
 Incomplete burning of waste - production of noxious gases, such
as carbon monoxide and nitrogen oxides.
 Solution-control the process to minimise their production.
 Countries where WTE industry not established-the cost of
converting waste to energy is higher than in other countries.
5
WTE Technologies
Thermo-chemical
conversion methods
Incineration
Combustion
Gasification
Pyrolysis
Bio-chemical
conversion methods
Microbial fuel cell(MFC)
Biomethanation
Biogas production from
landfills
6
THERMO –CHEMICAL
CONVERSION METHODS
7
Incineration
 Incineration is a thermal process - combustible components
thermally oxidized to produce heat energy
 Other products include bottom ash, fly ash, and flue gas, in
which are found a number of regulated pollutants
8
Incineration(contd..)
 Bottom ash is that component of the fuel not
converted to gas
 Comprised of inorganic materials -metal oxides and
unburned carbon ,remains in the char bed until
removed from the bottom of the combustor
 Smaller ash particles -entrained in the flue gas
removed along with VOCs &SVOCs and acid gas
constituents
9
Incineration(contd..)
 Several processes - removal of particulates from the
flue gas before released into atmosphere.
 Flue gas clean-up units commonly found in MSW
incineration plants include either a dry or wet acid gas
removal unit or scrubber, and a bag house
 For additional clean-up of the flue gas, carbon and/or
lime can be injected into the gas stream in the bag
house
10
Combustion
 Combustion is one of the oldest ways to convert fuel to
useful energy
 Combustion of biomass is a process in which oxygen reacts
with carbon in the fuel and produces carbon dioxide, water
and heat
 Gaseous combustion products include nitrogen oxidants,
carbon monoxide and aromatic compounds
 In a combustion reactor or furnace, raw material reacts with
oxygen in high temperature (> 800 °C) 11
Combustion(contd..)
 Initial step drying-followed by pyrolysis and gasification
 Final step : combustion where overall efficiency is highly
dependent on temperature, available O2 and raw material
properties
 Can be utilized to produce heat for households and for
industrial processes
 Simple example combustion of hydrogen and oxygen into
water vapour
12
Combustion(contd..)
 High-temperature exothermic redox chemical reaction between a
fuel and an oxidant usually atmospheric O2
 Combustion processes can be divided to batch and continuous
processes
 In households, wood-stove is a conventional batch combustion
process
 Combustion can also produce gaseous and liquid fuels
 Ash - utilized as fertilizer
 A complicated sequence of elementary radical reactions
13
Combustion(contd..)
 Quality of combustion can be improved by the designs
of combustion devices, such as burners and internal
combustion engines
 Further improvements are achievable by catalytic
converters
14
Gasification
 Controlled partial oxidation of a carbonaceous material
achieved by supplying less O2 than the stoichiometric
requirement
 central process between combustion and pyrolysis -proceeds
at temperatures ranging between 600 and 1500 0C
 widely used to produce commercial fuels and chemicals
 striking feature -ability to produce a reliable, high-quality
syngas product used for energy production
15
Gasification(contd..)
 Conventional fuels such as coal and oil, wastes :petroleum
coke, heavy refinery residuals, municipal sewage sludge
successfully used in gasification operations
 Process uses an agent, either air, O2, H2 or steam to convert
carbonaceous materials into gaseous products.
 First, the biomass is heated to around 600 degrees
 The volatile components, such as hydrocarbon gases,
hydrogen, CO, CO2, H2O and tar, vaporize by various
reactions 16
Gasification(contd..)
The remaining by-products are char and ash
For this first endothermic step, oxygen is not required
Second step, char is gasified by reactions with oxygen, steam
and hydrogen in high temperatures
endothermic reactions require heat, which is applied by
combusting some of the unburned char
Main products of gasification are synthesis gas, char and tars
17
Gasification(contd..)
 Gas mainly consists of CO, CO2,H2
 synthesis gas -utilized for heating or electricity
production
 Used for the production of ethanol, diesel and
chemical feedstocks
18
Pyrolysis
 Pyrolysis is thermal decomposition occurring in the absence
of oxygen
 First step in combustion and gasification processes followed
by total or partial oxidation of the heated material
 In the first step, temperature is increased to start the primary
pyrolysis reactions
 Volatiles are released and char is formed
 Finally pyrolysis gas is formed
19
Pyrolysis(contd..)
 The main product of slow pyrolysis is char or charcoal
 In slow pyrolysis biomass is heated to around 500 degrees for 5 to 30min
 Fast pyrolysis results mainly in bio-oil
 The biomass is heated in the absence of oxygen and the residence time
is 0.5 to 5s
 Vapors, aerosols and char are generated through decomposition
 After cooling bio-oil is formed
 The remaining non condensable gases used as a source of energy for the
pyrolysis reactor 20
BIO-CHEMICAL
CONVERSION METHODS
21
Microbial Fuel Cell(MFC)
 Devices that can use bacterial metabolism to produce
an electrical current from a wide range organic
substrates
 Electrons produced by the bacteria from these
substrates are transferred to the anode and flow to the
cathode linked by a conductive material containing a
resistor, or operated under a load
22
MFC (contd..)
23
MFC (contd..)
 Metal anodes consisting of non corrosive stainless steel mesh can
be utilized
 Copper is not useful due to the toxicity
 Most versatile electrode material is carbon, available as compact
graphite plates, rods, granules etc..
 (K3[Fe(CN)6]) electron acceptor in MFC
 Advantage of ferricyanide :low over potential using a plain
carbon cathode, resulting in a cathode working potential close to
its open circuit potential.
 Disadvantage: insufficient reoxidation by oxygen, which requires
the catholyte to be regularly replaced. 24
MFC (contd..)
 Can produce enough electricity to power ocean monitoring
devices
 Can work in marine settings when the anode is buried in
anaerobic marine sediments and cathode installed above the
sediment in the O2 rich water
25
Biomethanation
 Organic fraction of the waste is segregated and fed into a
closed container ie,biogas digester
 Digester- segregated waste undergoes biodegradation in
presence of methanogenic bacteria & under anaerobic
conditions, producing methane-rich biogas &effluent
 Biogas used either for cooking/heating applications, or for
generating motive power or electricity.
26
Biomethanation(contd..)
 Four key biological and chemical stages of anaerobic
digestion:
o Hydrolysis
o Acidogenesis
o Acetogenesis
o Methanogenesis
 Hydrolysis: can be merely biological (using hydrolytic
microorganisms) or combined: bio-chemical (using
extracellular enzymes), chemical (using catalytic reactions)
as well as physical (using thermal energy and pressure) in
nature
27
Biomethanation(contd..)
 Acetates and hydrogen produced in the first stages can be
used directly by methanogens
 Acidogenesis: further breakdown of the remaining
components by acidogenic (fermentative) bacteria
 Here VFA’s are generated along with CO2,NH3,H2S as well as
other by-products
28
Biomethanation(contd..)
 Acetogenesis: simple molecules created through the
acidogenesis phase are further digested by acetogens to
produce acetic acid as well as CO2 & H2
 Methanogenesis:methanogenic archaea utilise the
intermediate products of the preceding stages and convert
them into CO2,CH4,H2O
 The remaining, non-digestible organic and mineral material,
which the microbes cannot feed upon, along with any dead
bacterial residues constitutes solid digestate.
29
Biogas Production from Landfills
 Landfilling -primary method of disposal of municipal solid
waste and debris in the U.S. and many countries
 If left undisturbed, landfill waste produces significant
amounts of gaseous byproducts, consisting of CO2 &
CH4(greenhouse gases)
 increase the risk of climate change when they are released
unimpeded into the atmosphere
 CH4 -useful source of energy
30
Biogas Production from
Landfills(contd..)
 Landfill gas captured via collection system-consisting
of series of wells drilled into the landfill and connected
by a plastic piping system
 Gas burned directly in a boiler as a heat-energy source
 Biogas cleaned by removing water vapour and
sulphur dioxide, it can be used directly in internal-
combustion engines, or for electricity generation
31
Case Study(Solapur,Maharashtra)
Methodology
The municipal waste used in research was brought directly from the
waste dumping site
 MSW -high moisture content; it was contaminated and heterogeneous
in composition
 MSW -dried to reduce the moisture content in the material and shred
for size reduction
 waste was segregated manually for removal of recyclable materials,
stones and inorganic constituents
waste again separated through magnetic separation for removal of
ferrous and non-ferrous materials
MSW was shredded, classify and powdered 32
Case Study (contd..)
Before pelletization, municipal waste has to be processed for
size reduction, adding binder agents and reducing the
moisture content
 secondary shredding was carried out and pellets were
prepared by using PVC pipe size (2 inch X 15 cm)
 pellets were prepared by using starch as a binding agent
Calorific value of the pellet samples was measured by using
the acid digestion method and energy content was calculated
33
Case Study (contd..)
Results
 Municipal wastes -cheapest and easily available biomass
wastes, with no cost
 Calorific value of MSW after pelletization is high as
compared to parent composition waste
 MSW pellets :compact, economical have tremendous
market potential in non-coal producing zones
34
Review on WTE technology in
India
35
Conclusion
 Serve the dual purpose of managing solid waste and
generating energy from waste.
 Help in reducing green house gas emission thus preventing
global warming
 Helps in conserving land as land filling of waste requires
larger surface areas
 Earth Engineering Center at Columbia University and
National Environmental Engineering Research Institute have
decided to set-up Waste-to-Energy Research and Technology
Council (WTERT) in India
 responsible management of wastes based on science and best
available technology not on ideology and economics that
exclude environmental costs seem to be inexpensive now but
very costly in the future 36
References
1 .Boukelia and Mecibah(2012)“Solid waste as a renewable source of energy:
Current and future possibilities” International Journal of Energy and
Environmental Engineering
2.Mehtab Singh Chouhan et.al(2012) “Review on waste to energy potential in
India”
3.Chauhan Janardan Singh(2014) “International Journal of Chem Tech Research
4. R.Sunderesan et.al (2010) “Waste to Energy Generation from Municipal Solid
Waste in India”
5. Bary Wilson et.al(2013) “ A Comparative Assessment of Commercial
Technologies for Conversion of Solid Waste to Energy”
6.A.Bosmans et.al (2012) “The crucial role of waste to energy technologies in
landfill mining:a technological review”
7. Houran Li et.al (2007) “A state of art review on microbial fuel cells: A
promising technology for waste water treatment and bioenergy”
8. Preeti Jain et.al (2014) “Studies on Waste-to-Energy Technologies in India & a
detailed study of Waste-to-Energy Plants in Delhi”
9.M.Y Azwar et.al (2014) “Development of biohydrogen production by
photobiological, fermentation and electrochemical processes: A review”
37
THANK YOU
38

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Waste to energy

  • 1. WASTE TO ENERGY TECHNOLOGY REVIEWS IN INDIA Haritha M Assistant Professor Dept. of Civil Engg. 1
  • 2. Introduction  Form of energy recovery  Process of generating energy in the form of electricity or heat from primary treatment of waste  Waste-to-Energy means the use of modern combustion technologies to recover energy, usually in the form of electricity and steam  New technologies -reduce the volume of the original waste by 90%, depending upon composition and use of outputs 2
  • 3. Why we go for WTE?  Can address two sets of environmental issues at one stroke  Land use and pollution from landfills  Environmental perils of fossil fuels  Quite expensive  Some can be applied economically 3
  • 4. Major Constraints in WTE  Still a new concept in the country  Lack of financial resources with Municipal Corporations/Urban Local Bodies  Most of the proven and commercial technologies in respect of urban wastes are required to be imported  Lack of conducive policy guidelines from State Governments in respect of allotment of land, supply of garbage and power purchase 4
  • 5. Limitations of WTE  Waste low energy density than fossil fuels-cost of energy production increased-energy efficiency reduced  Locating the waste processing plant near the waste resources reduce problem  Incomplete burning of waste - production of noxious gases, such as carbon monoxide and nitrogen oxides.  Solution-control the process to minimise their production.  Countries where WTE industry not established-the cost of converting waste to energy is higher than in other countries. 5
  • 6. WTE Technologies Thermo-chemical conversion methods Incineration Combustion Gasification Pyrolysis Bio-chemical conversion methods Microbial fuel cell(MFC) Biomethanation Biogas production from landfills 6
  • 8. Incineration  Incineration is a thermal process - combustible components thermally oxidized to produce heat energy  Other products include bottom ash, fly ash, and flue gas, in which are found a number of regulated pollutants 8
  • 9. Incineration(contd..)  Bottom ash is that component of the fuel not converted to gas  Comprised of inorganic materials -metal oxides and unburned carbon ,remains in the char bed until removed from the bottom of the combustor  Smaller ash particles -entrained in the flue gas removed along with VOCs &SVOCs and acid gas constituents 9
  • 10. Incineration(contd..)  Several processes - removal of particulates from the flue gas before released into atmosphere.  Flue gas clean-up units commonly found in MSW incineration plants include either a dry or wet acid gas removal unit or scrubber, and a bag house  For additional clean-up of the flue gas, carbon and/or lime can be injected into the gas stream in the bag house 10
  • 11. Combustion  Combustion is one of the oldest ways to convert fuel to useful energy  Combustion of biomass is a process in which oxygen reacts with carbon in the fuel and produces carbon dioxide, water and heat  Gaseous combustion products include nitrogen oxidants, carbon monoxide and aromatic compounds  In a combustion reactor or furnace, raw material reacts with oxygen in high temperature (> 800 °C) 11
  • 12. Combustion(contd..)  Initial step drying-followed by pyrolysis and gasification  Final step : combustion where overall efficiency is highly dependent on temperature, available O2 and raw material properties  Can be utilized to produce heat for households and for industrial processes  Simple example combustion of hydrogen and oxygen into water vapour 12
  • 13. Combustion(contd..)  High-temperature exothermic redox chemical reaction between a fuel and an oxidant usually atmospheric O2  Combustion processes can be divided to batch and continuous processes  In households, wood-stove is a conventional batch combustion process  Combustion can also produce gaseous and liquid fuels  Ash - utilized as fertilizer  A complicated sequence of elementary radical reactions 13
  • 14. Combustion(contd..)  Quality of combustion can be improved by the designs of combustion devices, such as burners and internal combustion engines  Further improvements are achievable by catalytic converters 14
  • 15. Gasification  Controlled partial oxidation of a carbonaceous material achieved by supplying less O2 than the stoichiometric requirement  central process between combustion and pyrolysis -proceeds at temperatures ranging between 600 and 1500 0C  widely used to produce commercial fuels and chemicals  striking feature -ability to produce a reliable, high-quality syngas product used for energy production 15
  • 16. Gasification(contd..)  Conventional fuels such as coal and oil, wastes :petroleum coke, heavy refinery residuals, municipal sewage sludge successfully used in gasification operations  Process uses an agent, either air, O2, H2 or steam to convert carbonaceous materials into gaseous products.  First, the biomass is heated to around 600 degrees  The volatile components, such as hydrocarbon gases, hydrogen, CO, CO2, H2O and tar, vaporize by various reactions 16
  • 17. Gasification(contd..) The remaining by-products are char and ash For this first endothermic step, oxygen is not required Second step, char is gasified by reactions with oxygen, steam and hydrogen in high temperatures endothermic reactions require heat, which is applied by combusting some of the unburned char Main products of gasification are synthesis gas, char and tars 17
  • 18. Gasification(contd..)  Gas mainly consists of CO, CO2,H2  synthesis gas -utilized for heating or electricity production  Used for the production of ethanol, diesel and chemical feedstocks 18
  • 19. Pyrolysis  Pyrolysis is thermal decomposition occurring in the absence of oxygen  First step in combustion and gasification processes followed by total or partial oxidation of the heated material  In the first step, temperature is increased to start the primary pyrolysis reactions  Volatiles are released and char is formed  Finally pyrolysis gas is formed 19
  • 20. Pyrolysis(contd..)  The main product of slow pyrolysis is char or charcoal  In slow pyrolysis biomass is heated to around 500 degrees for 5 to 30min  Fast pyrolysis results mainly in bio-oil  The biomass is heated in the absence of oxygen and the residence time is 0.5 to 5s  Vapors, aerosols and char are generated through decomposition  After cooling bio-oil is formed  The remaining non condensable gases used as a source of energy for the pyrolysis reactor 20
  • 22. Microbial Fuel Cell(MFC)  Devices that can use bacterial metabolism to produce an electrical current from a wide range organic substrates  Electrons produced by the bacteria from these substrates are transferred to the anode and flow to the cathode linked by a conductive material containing a resistor, or operated under a load 22
  • 24. MFC (contd..)  Metal anodes consisting of non corrosive stainless steel mesh can be utilized  Copper is not useful due to the toxicity  Most versatile electrode material is carbon, available as compact graphite plates, rods, granules etc..  (K3[Fe(CN)6]) electron acceptor in MFC  Advantage of ferricyanide :low over potential using a plain carbon cathode, resulting in a cathode working potential close to its open circuit potential.  Disadvantage: insufficient reoxidation by oxygen, which requires the catholyte to be regularly replaced. 24
  • 25. MFC (contd..)  Can produce enough electricity to power ocean monitoring devices  Can work in marine settings when the anode is buried in anaerobic marine sediments and cathode installed above the sediment in the O2 rich water 25
  • 26. Biomethanation  Organic fraction of the waste is segregated and fed into a closed container ie,biogas digester  Digester- segregated waste undergoes biodegradation in presence of methanogenic bacteria & under anaerobic conditions, producing methane-rich biogas &effluent  Biogas used either for cooking/heating applications, or for generating motive power or electricity. 26
  • 27. Biomethanation(contd..)  Four key biological and chemical stages of anaerobic digestion: o Hydrolysis o Acidogenesis o Acetogenesis o Methanogenesis  Hydrolysis: can be merely biological (using hydrolytic microorganisms) or combined: bio-chemical (using extracellular enzymes), chemical (using catalytic reactions) as well as physical (using thermal energy and pressure) in nature 27
  • 28. Biomethanation(contd..)  Acetates and hydrogen produced in the first stages can be used directly by methanogens  Acidogenesis: further breakdown of the remaining components by acidogenic (fermentative) bacteria  Here VFA’s are generated along with CO2,NH3,H2S as well as other by-products 28
  • 29. Biomethanation(contd..)  Acetogenesis: simple molecules created through the acidogenesis phase are further digested by acetogens to produce acetic acid as well as CO2 & H2  Methanogenesis:methanogenic archaea utilise the intermediate products of the preceding stages and convert them into CO2,CH4,H2O  The remaining, non-digestible organic and mineral material, which the microbes cannot feed upon, along with any dead bacterial residues constitutes solid digestate. 29
  • 30. Biogas Production from Landfills  Landfilling -primary method of disposal of municipal solid waste and debris in the U.S. and many countries  If left undisturbed, landfill waste produces significant amounts of gaseous byproducts, consisting of CO2 & CH4(greenhouse gases)  increase the risk of climate change when they are released unimpeded into the atmosphere  CH4 -useful source of energy 30
  • 31. Biogas Production from Landfills(contd..)  Landfill gas captured via collection system-consisting of series of wells drilled into the landfill and connected by a plastic piping system  Gas burned directly in a boiler as a heat-energy source  Biogas cleaned by removing water vapour and sulphur dioxide, it can be used directly in internal- combustion engines, or for electricity generation 31
  • 32. Case Study(Solapur,Maharashtra) Methodology The municipal waste used in research was brought directly from the waste dumping site  MSW -high moisture content; it was contaminated and heterogeneous in composition  MSW -dried to reduce the moisture content in the material and shred for size reduction  waste was segregated manually for removal of recyclable materials, stones and inorganic constituents waste again separated through magnetic separation for removal of ferrous and non-ferrous materials MSW was shredded, classify and powdered 32
  • 33. Case Study (contd..) Before pelletization, municipal waste has to be processed for size reduction, adding binder agents and reducing the moisture content  secondary shredding was carried out and pellets were prepared by using PVC pipe size (2 inch X 15 cm)  pellets were prepared by using starch as a binding agent Calorific value of the pellet samples was measured by using the acid digestion method and energy content was calculated 33
  • 34. Case Study (contd..) Results  Municipal wastes -cheapest and easily available biomass wastes, with no cost  Calorific value of MSW after pelletization is high as compared to parent composition waste  MSW pellets :compact, economical have tremendous market potential in non-coal producing zones 34
  • 35. Review on WTE technology in India 35
  • 36. Conclusion  Serve the dual purpose of managing solid waste and generating energy from waste.  Help in reducing green house gas emission thus preventing global warming  Helps in conserving land as land filling of waste requires larger surface areas  Earth Engineering Center at Columbia University and National Environmental Engineering Research Institute have decided to set-up Waste-to-Energy Research and Technology Council (WTERT) in India  responsible management of wastes based on science and best available technology not on ideology and economics that exclude environmental costs seem to be inexpensive now but very costly in the future 36
  • 37. References 1 .Boukelia and Mecibah(2012)“Solid waste as a renewable source of energy: Current and future possibilities” International Journal of Energy and Environmental Engineering 2.Mehtab Singh Chouhan et.al(2012) “Review on waste to energy potential in India” 3.Chauhan Janardan Singh(2014) “International Journal of Chem Tech Research 4. R.Sunderesan et.al (2010) “Waste to Energy Generation from Municipal Solid Waste in India” 5. Bary Wilson et.al(2013) “ A Comparative Assessment of Commercial Technologies for Conversion of Solid Waste to Energy” 6.A.Bosmans et.al (2012) “The crucial role of waste to energy technologies in landfill mining:a technological review” 7. Houran Li et.al (2007) “A state of art review on microbial fuel cells: A promising technology for waste water treatment and bioenergy” 8. Preeti Jain et.al (2014) “Studies on Waste-to-Energy Technologies in India & a detailed study of Waste-to-Energy Plants in Delhi” 9.M.Y Azwar et.al (2014) “Development of biohydrogen production by photobiological, fermentation and electrochemical processes: A review” 37