Anaerobic Wastewater Treatment for Energy Recovery and Emission Reduction : TNPL Case Study
Dr. S.CHINNARAJ Dr S CHINNARAJ Research and Development Division Tamilnadu Newsprint and Papers Ltd Kagithapuram, Karur TN- 639 136 TNbiotech@tnpl.co.in
International Training Course on Bio-Energy BioMarch 19 – 31, 2006 31 Indian Institute of Science, Bangalore (Sponsored by MNES, Government of India)
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Anaerobic Wastewater Treatment for Energy Recovery and Emission Reduction : TNPL Case Study 1. About TNPL g 2. Anaerobic Digestion 3. Greenhouse Effect and Climate Change 4. 4 Biomethanation & Climate Change 5. Biomethanation In TNPL
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Anaerobic Wastewater Treatment for Energy Recovery and Emission Reduction : TNPL Case Study
1. About TNPL
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About TNPL
• • • • • • Promoted by the Govt. of Tamil Nadu during early eighties to manufacture Newsprint & fine paper using bagasse as primary raw material The largest bagasse based paper mill in the World. Consumes one million MT of bagasse every year Commenced the commercial production with a capacity of 90,000 tpa in 1985 Increased the capacity to 1,80,000 tpa in 1996 by installing the second paper machine. hi Capacity increased to 2,30,000 tpa in 2002 through upgrade of paper machines As continual improvement, TNPL embarked on a Mill development plan at improvement a cost of Rs.565 Crores to become environmentally benign by implementing Elemental Chlroine Free (ECF) bleaching sequence in the inhouse pulping lines
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TAMIL NADU NEWSPRINT AND PAPERS LIMITED Kagithapuram, Tamil Nadu
Tamilnadu Newsprint and Papers Ltd.
Tamilnadu Newsprint and Papers Ltd.
Tamilnadu Newsprint and Papers Ltd.
Tamilnadu Newsprint and Papers Ltd.
Tamilnadu Newsprint and Papers Ltd.
Tamilnadu Newsprint and Papers Ltd.
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Tamilnadu Newsprint and Papers Ltd.
Anaerobic Wastewater Treatment for Energy Recovery and Emission Reduction : TNPL Case Study
2. Anaerobic Digestion
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Why Anaerobic Digestion !
Biodegradable pollutants in the wastewater are converted to biogas containing methane carbon dioxide and methane, biomass (little) in the absence of oxygen by Anaerobic microorganisms
5% 10% Biomass Effluent
Organic Pollutants Anaerobic Microbes CH4, CO2 H2S
+
New Cells
Net energy surplus is generated during AD in the form of CH4 bearing biogas
85% CH4/CO2
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Metabolic Stages of Anaerobic Digestion
Polymers (Proteins, Polysaccharides) 1 Monomers (Sugars, Amino acids, Peptides) 2 2 Propionate, Butyrate H2 + CO2 4 3 3 3 Acetate A t t 4 2
1. Hydrolytic Bacteria 2. Fermentative Bacteria 3. Acetogenic Bacteria 4. Methanogenic Bacteria
CH4 + CO2
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Types of Anaerobic Reactors
Low rate anaerobic reactors High rate anaerobic reactors
Anaerobic contact process Anaerobic Lagoon Septic tank Standard rate anaerobic digester
Slurry type bioreactor, temperature, mixing, SRT or other environmental conditions are not regulated. . loading of 1-2 kg COD/m3-day.
Anaerobic filter (AF) Upflow anaerobic sludge Blanket (UASB) Fluidized bed Reactor Hybrid reactor: UASB/AF
Able to retain very high concentration of active biomass in the reactor. Thus extremely high SRT could be maintained irrespective of HRT. Load 5-20 kg COD/m3-d HRT 5 20 d COD removal efficiency : 80-90%.
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Upflow Anaerobic Sludge Blanket (UASB)
UASB was developed in 1970s by Dr. G. Lettinga in the N th l d th Netherlands It is a special kind of reactor concept for high rate anaerobic treatment of wastewater t bi t t t f t t It is essentially a suspended growth system in which proper hydraulic and organic loading rate hi h h d li d i l di is maintained in order to facilitate the formation of granules The granules consist of hydrolytic bacteria, acidogen/acetogens and methanogens id / d h
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UASB REACTOR
Biogas
Settler Baffle
Weir for effluent collection
Rising gas bubble Sludge bed Influent Influent distributor
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Essential Conditions for Anaerobic Treatment
1. No excessive air/O2 exposure, pH (6.8 - 7.8), Temp. Temp 30 to 38oC, Alkalinity >1500 ppm C 2. No toxic/inhibitory compounds in the influent 3. Enough nutrients (COD:N:P = 500:7:1) and trace metals especially, Fe, Co, Ni, etc. t t l i ll F C Ni t
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Best Candidates of Industrial Wastewater for Anaerobic Treatment
• • •
Alcohol production & Brewery Sugar processing Starch (barley, corn, potato, wheat, tapioca) and desizing waste from textile industry industry. Food processing & Slaughter house Pulp and paper p p p Petrochemical waste
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• • •
Process Advantage
1. Less energy requirement, because no aeration is needed e gy generation the o of et a e 2. Energy ge e at o in t e form o methane gas 3. Less biomass (sludge) generation ( ) q 4. Less nutrients (N & P) requirement because of low biomass 5. Higher organic loading rate 6. Space saving due to high organic loading
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Limitations of Anaerobic Process
1. Long start-up time due to low biomass yield start2. Long recovery time due to low biomass y g y yield 3. Specific nutrients/trace metal requirements 4. 4 More susceptible to pH temperature and pH, redox potential 5. Quality of treated wastewater
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Anaerobic Wastewater Treatment for Energy Recovery and Emission Reduction : TNPL Case Study
3. Greenhouse Effect and Climate
Change
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Greenhouse Effect
Greenhouse gases keep IR from transmitting directly out to space
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GHG in Atmosphere
GHG Name Carbon –di- Oxide diMethane Nirous Oxide CFCCFC-12 HCFCHCFC-22 Perfluromethane PrePre-industrial Concentrat life time GWP Concentration i in 1994 ( C t ti ion i (years) ) 278 ppmv 700 ppbv 275 ppbv 0 0 0 377 ppmv 1783 ppbv 318 ppbv Variable 1 12.2 120 21 310 6200-7100 62001300-1400 13006500 23900
0.503 ppbv 102 0.105 ppbv 12.1 0.070 ppbv 50000 0.032 ppbv 3200 0 032
Sulphur hexa-fluride 0 hexa-
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CO2 in Atmosphere
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GHG and Global Warming
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Atmosphere is warming ?
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Impacts
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International Efforts
United Nations Framework Convention on Climate Change (UNFCCC) • • • Ultimate objective of stabilizing global greenhouse gas concentrations in the atmosphere Developed countries (Annex I countries) aim to restore GHG emissions to 1990 levels and less Support capacity building in, and facilitate technology transfer to developing countries to mitigate, and to adapt to climate change
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Polluter Should Pay
Annex I
Non-Annex N A
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Promises Made
Kyoto Protocol: 36 Developed Countries and Economies in Transition (namely Canada Japan European Union and most Canada, Japan, East European countries) agree to: • • • • • Reduce GHG emissions by 5.2 % below 1990 levels in the y commitment period 2008-2012 2008Marrakech Accord: agreed in Nov 2001 sets rules of implementation Required ratification of 55 Parties to UNFCCC representing 55 % of CO2 emissions from developed countries Came into force February 16, 2005 As of February 2006, 162 states ratified representing 66.1% developed countries emission
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Solutions !
How can Developed Countries/EITs meet their obligations under Kyoto?
•
Domestic Emission Reductions a d o est y activities ( and forestry act t es (limited to ~330 Mt/CO2e) ted 330 t/CO
• Carbon Sinks: Direct human-induced land use change human• International Emissions Trading • Project Based: Joint Implementation j p Clean Development Mechanism
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Market Based Mechanism !
Trade of Emission Allowances
Carbon Transactions
Joint J i t Implementation (JI)
ProjectProject-Based Transactions
Clean Development Mechanisms (CDM)
NonNon-Kyoto Projects
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Type of Projects
1. Installations b 1 I t ll ti based on renewable energy (Geo thermal, wind, d bl (G th l i d solar, biomass, small hydro etc.) 2. Fuel switch to lower carbon intensive fuels (electricity, heat sector) 3. Combined heat and power projects 4. Transport sector 5. Land fills gas recovery (methane emission avoidance & use) 6. Waste & Wastewater handling (methane emission avoidance and use) se) 7. Reforestation and Afforestation (A/R) projects (carbon sequestration).
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Project Cycle
• • • • • •
Project Design Validation / Registration Monitoring g Verification / Certification CER Issuance
Project Participant (PP) Designated Operating Entity (DOE) Executive Board Project Participant (PP) j p ( ) Designated Operating Entity (DOE) Executive Board (EB)
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Registered Projects by Country y
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CERs from Registered Projects by Country
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Registered Projects by Sector
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Energy distrib b. Transport Tidal EE Service N2O EE Households
CDM Projects in Pipeline
G eothermal Solar Fugitive HFCs Cement Biogas Fossil fuel sw witch Landfill gas Agriculture Wind EE Industry Hydro Biomass ene rgy
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80 60 40 140 120 100 20 0
Anaerobic Wastewater Treatment for Energy Recovery and Emission Reduction : TNPL Case Study
4. Biomethanation & Climate Change
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Methane and Climate Change
Methane: Most abundant greenhouse gas after CO2 in the atmosphere Concentrations is increasing from pre -industrial times (now :1783 ppbv) 23 times more Global warming potential than CO2
Contribution to Global Warming
HaloHalo-carbons 18% N2O 6%
CH4 19%
CO2 57%
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Methane in Atmosphere
GHG Increase From 1750 CO2 :35% CH4 :155% N2O :18%
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Anaerobic Treatment for Emission or Energy ? gy
Conventional Uncontrolled Anaerobic Digestion Controlled Anaerobic Digestion (UASB)
Reduced CO2 Emission
85% CH4 /CO2 Emission
Reduced Fuel use
No CH4 Emission
Power Plant, Lime kiln Anaerobic Reactor (5% Bi Biomass) )
Organics in wastewater
Anaerobic Lagoon (Biomass 5%)
10 % in effluent
Organics in Wastewater
10 % in Effluent
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Anaerobic Wastewater Treatment for Energy Recovery and Emission Reduction : TNPL Case Study
5. Biomethanation In TNPL
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TNPL ETP Process Flow g Diagram
Bagasse Handling and Preparation
Screens
Bag. ag Clarifier
Anaerobic UASB Lagoon
process
Primary Clarifier 2
Pulp-mill PM/c & Others
Screens
Primary Clarifier I
Activated Sludge Lagoon L
Sec. Clarifier
SLUDGE FOR DISPOSAL
SLUDGE DEWATERING
Sludge Thickener
TO IRRIGATION
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TNPL Biogas Process Flow Diagram g
Lime-Kiln
Gas Holder
UASB Reactor A
UASB Reactor B
MOL Tank
Bag. Wash Wastewater
Equal. Tank
Neutral. Tank
Clarifier
Buffer Tank
Nut.
Tank
Sludge for Disposal
Decanter Centrifuge
Sludge Pit
Treated Effluent To ASL
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Biogas Plant Design
COD Load Hydraulic Retention Time Reactor Volume Volumetric Loading Rate COD Reduction Gas Production Factor Gas Production Flow : 57.6 T/Day : 20 hrs : 2 X 5,000 m3 : 6.0 kg COD/m3/Day : 85% : 0.47 m3/kgCODr y : 23,000 m3/Day : 12,000 m3/Day
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Biogas Plant Performance
Wastewater Ttreated in m
4,000,000 1 1416150 0 29 947476
3
2,000,000
-
2003
2004
2005
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3 146900
Biogas Plant Performance
COD Reduced in MT
11106 6 15000 10000 5000 0 4716 8 8686
2003
2004
2005
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Biogas Plant Performance
Biogas Produced in m
6,000,000 4,000,000 2,000,000 2 000 000 2 2,374,64 42 3,507 7,891
3
2003
2004
2005
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4, 752,592 2
Biogas Plant Performance
Oil Saving in kL S i i
2009 3000 2000 1000 0 1450 2849
2003
2004
2005
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CDM Project Status
Methane Extraction and Fuel Conservation Project ( g j (High rate Bio-Methanation) Bio• Estimated CERs Generation 37 000 t CO2e y -1 37,000 Project Identification Project Design Document (PDD) Host Country approval (2nd May 2005) Validation Registration (14th January 2006) Verification CER t di trading
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Emission Calculation
Methodology Adopted :
Emission Reductions t CO2e
AM0013 / Version 02
Project Emissions t CO2e
Baseline Emissions t CO2e
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Baseline Emissions
1. CH4 emission from open anaerobic lagoons
Total COD to lagoon
Maximum CH4 producing capacity
CH4 conversion factor
2. Emission from Fossil fuel combustion
Mass conversion factor
Biogas used
Energy Content of biogas
Carbon Content of Fuel
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Baseline Emission t CO2e
18 54,21
2005
40,000 18,2 289 30,000 20,000 10,000 2003
2,925 22
33,46 68
50,000
40 ,469
4 44,791
60,000
4 4,636
2004
Open Lagoon
Fossil Fuel
7,001
Total
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9,427
Project Emissions
1. CH4 emission from open anaerobic lagoons
Total undigested COD to lagoon
Maximum CH4 producing capacity
CH4 conversion factor
2. Emission due to leakage
Physical leakage from digester g
Emission from electricity consumption
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Project Emission t CO2e
20,000
10890
15,000 , 10,000
2 ,9 4 2
8 ,6 4 6
5959
5 ,1 9 9
5,000 -
2743
5020
2003
274
2004
671
Open Lagoon O L
Electricity C El t i it Consump
Physical L k Ph i l Leakage
750
2005
6719
16115
Total T t l
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Emission Reduction t CO2e
60,000
40, ,469 54,218
65 16,96
20,000 10,000 -
2003
5 5,959
2004
10,890
2005
Baseline B li
Project P j t
Emission R d ti E i i Reduction
Tamilnadu Newsprint and Papers Ltd.
16,11 15
30,000
22 2,925
29,579
40,000
38,1 103
50,000
CER Generated from Aug. 2003 – Dec. 2005
100,000 80,000 80 000 29,5 579 60,000 40,000 20,000 16,965 5 38 8,103
2003
2004
2005
Total
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84,648
Conclusion
The plant generates around 13,000 to 15,000 M3 of biogas with COD reduction of around 83 - 85 % I. Environmental Benefits from Aug. 03 to Dec. 05 • • • • • COD Reduced GHG Reduced Biogas generated Furnace oil Saving CERs CER generated t d :24,500 t :85,000 t CO2e :85 000 :10.64 :10 64 million m3 : 6308 t :85,000 85 000
II. Economical Benefits from Aug. 03 to Dec. 05
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Thank You for Your Attention Any Questions ?
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