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ISWA
Ir. M.A.J. (Marcel) van Berlo
Waste & Energy CompanyCity of [email protected]
Value from Waste
Amsterdam’s Vision on the 4th-generation Waste-2-Energy
ISWA congress 2007Plant Visit at Afvalenergiebedrijf
Amsterdam, 27 september 2007
ISWA
1. INTRODUCTION1. INTRODUCTION
1. Introduction2. Scenarios for Recovery 3. Amsterdam4. New generation of waste incineration5. Conclusion
1. Introduction2. Scenarios for Recovery 3. Amsterdam4. New generation of waste incineration5. Conclusion
Gemeente AmsterdamAfval Energie Bedrijf
SocietySociety
Raw materials
Air
Water Waste Water
Waste
Exhaust
Society
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Closing the loopClosing the loop
Waste
Energy
Air
Water Waste Water
Exhaust gas
Society
WFPPRaw materials
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DesertDesert
• Scarcity• Survival• Self supporting• Deterrence• Robustness• Long live cycle• Economical (=Zuinig)
• Waste prevention• Residues remain
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Tropical rain forest:Tropical rain forest:
• Abundance• Growth• Competition• Complexity• Redundancy • Short life-cycle• Wasteful (=Verspillend)
• Massive disposal• Massive recycling: 1. Eat-and-be-eaten =
use the proteins2. Down cycle =
Molecular decomposition3. Production =
from residues
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Grades of recyclingGrades of recyclingSociety
Reuse: “as-is or repair”
Disassemble: “components”
Fragment: “materials”
Decompose: “Molecules”
Convert: “Atoms and energy”
Second hand car
Dismantling the car
Shredder
Fermentation, Pyrolysis
Burn
Raw materials Waste
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Waste is a RENEWABLE !Waste is a RENEWABLE !
l 100% Sustainable Energy from an endlessflow of waste
l 50% Renewable CO2-free energyfrom biomass
l 100% Sustainable Energy from an endlessflow of waste
l 50% Renewable CO2-free energyfrom biomass
l Richer than most RAW MATERIALShigh concentration of valuable METALS
l Richer than most RAW MATERIALShigh concentration of valuable METALS
WasteFired
PowerPlant
RenewableENERGY
50% of waste is BIOMASS
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2. Dutch scenario 20122. Dutch scenario 2012
0
10
20
30
40
50
60
70
Not CombustibleCombustibleReuse
0
10
20
30
40
50
60
70
Not CombustibleCombustibleReuse
Total Waste Production
0
2
4
6
8
10
12
2002 2012
Landfill Other waste incineration R1 Hazardous waste R1 Sludges D10 Incineration D10
0
2
4
6
8
10
12
2002 2012
Landfill Other waste incineration R1 Hazardous waste R1 Sludges D10 Incineration D10
Combustible Waste
MTon/year
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Dutch Results of policyDutch Results of policy
0
1020
30
40
5060
70
1985
1988
1991
1994
1997
2000
2003
Mto
n/ye
ar
Reuse/Recycling
Incineration
Discharge
Landfill
ISWA
Dutch waste policy
Instruments for steering waste management:Regulations on landfill (1980-90)Legislation- stringent emission limits incineration(1990) - directives and covenants (glass, paper, CFK)
Ban on landfill and landfill tax for combustible waste (1995)Financial incentives (REB 1997, MEP 2005)
Preference order:1. Prevention2. Reuse and Recycling3. Incineration/energy production4. Landfill
ISWA
Cost ranges for Waste Management options
2050 30
150
30
200
110
80
0
50
100
150
200
Landfill Incineration Reuse/recycling
€ / t
on M
SW
Landfill TaxMaximum cost rangeMinimum cost
Price competition versus Preference order
Cheap landfill beats every other optionLandfill tax (or landfill ban) is needed to give reuse/recycling a fair chanceWtE (as alternative for land filling) is needed to implement landfill taxesPrices of incineration are within range of reuse/recycling optionsCountries with high WtE percentage have much better reuse/recycling percentage
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2. SCENARIOS: “Integral chain efficiency”2. SCENARIOS: “Integral chain efficiency”
PaperGlass
HouseholdEnergy
30%WFPP30%
Separation(mechanical)
Energy28%
Overall efficiency
Conversion efficiency
30%
Percent of Mass RDF
40%
25%Landfill
Energy2%
25%
20%
Digestion5%
recovery Material
Source
PaperGlass
Landfill 1,5%
MaterialsSAI
The NEW Generation WtE
Third generation (1985-now) is “designed to be CLEAN”
Fourth generation (now--> ….) is“designed for RECOVERY”
of ENERGY and MATERIALS
Third generation (1985-now) is “designed to be CLEAN”
Fourth generation (now--> ….) is“designed for RECOVERY”
of ENERGY and MATERIALS
2. PERFORMANCE INDICATORS for WtE2. PERFORMANCE INDICATORS for WtE
Energy LCA,GHG-emission/
avoidance,LCCMass
Dust, NOx, CO, HCl, SO2, CxHy dioxin, HM, CO2
Deviation rate
R1/D10,Exergy,Primary-
resources
Output Quantity Effect Evaluation
Acidity, Toxicity,CO2-equiv
WasteWtE
Electricity
Exhaust gas
Residues
Heat
Materials
Input
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RECOVERY is the new RULE !RECOVERY is the new RULE !
It was WI Waste incineration
It is WTE Waste To Energy
It will be WFPP Waste Fired Power Plant
It was WI Waste incineration
It is WTE Waste To Energy
It will be WFPP Waste Fired Power Plant
ca. 15%
30%
ca. 15%
30%
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Electrical Efficiency of Power PlantsElectrical Efficiency of Power Plants
Depends on fuel quality:
l Natural Gas 55 %l Oil 50 %l Coal 45 %l Lignite 40 %l Biomass 35 %
l Waste 15…22 %....30%
Depends on fuel quality:
l Natural Gas 55 %l Oil 50 %l Coal 45 %l Lignite 40 %l Biomass 35 %
l Waste 15…22 %....30%
Current:State-of-the-Art
Current:State-of-the-Art
New:Best Available Technology
New:Best Available Technology
Current AverageCurrent Average
EXergy ProductionEXergy Production
0,0%
5,0%
10,0%
15,0%
20,0%
25,0%
30,0%
35,0%
40,0%
45,0%
50,0%
Exergy equ.Recovered metals
Exergy efficiency
Exergy equ. Recovered metals 0,0% 0,0% 4,5% 7,0% 10,8% 7,0% 10,8% 4,5%
Exergy efficiency 0,0% 2,0% 14,6% 19,8% 30,0% 24,5% 33,1% 14,6%
DUMPSITELANDFILL+
biogas engines
WtE Average NL
WtE Convention
al
WtE Optimised
WtE Conv.+CHP
WtE Optim.+CH
P
WtE heat only
R1 / D10 (with proposed limits)R1 / D10 (with proposed limits)
00,05
0,84
0,630,5
0,91 0,88
1,11
0,6 0,65
0
0,2
0,4
0,6
0,8
1
1,2
DU
MPSITE
LAN
DFILL
WtE
Average
WtE C
onv.
WtE O
ptim.
WtE
Conv.+C
HP
WtE
Optim
.+CH
P
WtE heatonly
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3. Amsterdam: Waste & Energy Enterprise
3. Amsterdam: Waste & Energy Enterprise
l Owned by Local governmentl Long term contractsl Commercial operation: 70 €/ton of wastel Capital intensivel Industrial scalel Mission: Maximise the use of wastel Ambitious targets
- Best environmental performance- Lowest cost
l Owned by Local governmentl Long term contractsl Commercial operation: 70 €/ton of wastel Capital intensivel Industrial scalel Mission: Maximise the use of wastel Ambitious targets
- Best environmental performance- Lowest cost
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Generations in Waste incinerationGenerations in Waste incineration
Generation Capacity [ton/year] Operational paradigm
1885 - Open air incineration
1st 1917 150.000 Hygiene
2nd 1969 500.000 Flue gas de-dusting
3rd 1993 800.000 Chemical cleaning
4th 2006 + 500.000 RECOVERYof ENERGY and MATERIALS
Generation Capacity [ton/year] Operational paradigm
1885 - Open air incineration
1st 1917 150.000 Hygiene
2nd 1969 500.000 Flue gas de-dusting
3rd 1993 800.000 Chemical cleaning
4th 2006 + 500.000 RECOVERYof ENERGY and MATERIALS
Start collectionStart collection
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1st Incineration 1919-19691st Incineration 1919-1969
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AVI-Noord 1969-1993AVI-Noord 1969-1993
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Aerial picture (overview)Aerial picture (overview)
Gemeente AmsterdamAfval Energie Bedrijf
Construction of WFPP in AmsterdamConstruction of WFPP in Amsterdam
ISWA
Generations Waste to Energy in Amsterdam
0
200.000
400.000
600.000
800.000
1.000.000
1.200.000
1.400.000
1.600.000
1.800.000
2.000.000
1915
1920
1925
1930
1935
1940
1945
1950
1955
1960
1965
1970
1975
1980
1985
1990
1995
2000
2005
Waste[Tons/Year]
0
100.000
200.000
300.000
400.000
500.000
600.000
700.000
800.000
900.000
1.000.000
Elektricity[MWh/Year]
HR-AEC
AEC - slib
AEC - afval
AVI-Noord2
AVI-Noord1
E-productie
4e
1e
2e
3e
4e
3e
2e
1e
Amsterdam waste and Energy production
Gemeente AmsterdamAfval Energie Bedrijf
SIZE MATTERSInvestment in relation to the capacity of 4 Dutch AVI’sSIZE MATTERSInvestment in relation to the capacity of 4 Dutch AVI’s
0
500
1000
1500
2000
100 200 300 400 500 600 700 800 900Capacity in 1000 ton / year
0
500
1000
1500
2000
100 200 300 400 500 600 700 800 900Capacity in 1000 ton / year
AVI AmsterdamAVI Amsterdam
InvestmentInvestment
in in €€ perper
ton / ton / yearyear
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4. New generation in Waste incineration4. New generation in Waste incineration
Historical waste incineration “generations”:
l 0 Open air incineration
l 1st 1900 oven
l 2nd 1960 dust removal from flue gas
l 3rd 1985 chemical cleaning of flue gas
In this presentation we outline a new step:l 4th 2006 RECOVERY
of energy and materials
Historical waste incineration “generations”:
l 0 Open air incineration
l 1st 1900 oven
l 2nd 1960 dust removal from flue gas
l 3rd 1985 chemical cleaning of flue gas
In this presentation we outline a new step:l 4th 2006 RECOVERY
of energy and materials
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Why new generation ?Why new generation ?
RECOVERY is the“next logical step”.
RECOVERY is the“next logical step”.
Historical development of public awareness:Historical development of public awareness:
A newly identified need leads to
a new technical concept.
A newly identified need leads to
a new technical concept.
The adapted installations will have additional lifetime because of social acceptability
The adapted installations will have additional lifetime because of social acceptability
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4th-generation Incineration4th-generation Incinerationl Cost must go down l Reliable, proven technology
l Energy Optimisation to the max !!Leap from 22% to >30%
l Material reuse to the max !!Fe, Al, Cu, Gypsum, CaCl2,Washed bottom ash = N1 quality building materialWashed fly ash = inert
l Cost must go down l Reliable, proven technology
l Energy Optimisation to the max !!Leap from 22% to >30%
l Material reuse to the max !!Fe, Al, Cu, Gypsum, CaCl2,Washed bottom ash = N1 quality building materialWashed fly ash = inert
= WFPP= WFPP
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CONCEPT for RECOVERYCONCEPT for RECOVERY
Incineration Fluegasscleaning
Chemicals 10 kgChemicals 10 kg
FluegassFluegass
Municipal Municipal SolidSolidWasteWaste
850850 kWh/tonkWh/ton = = 3030 %% of energy in wasteof energy in waste
Salt 7 kgGypsum 5 kgFly-ash 10 kgResidueResidue 55 kgkg
Non Ferro 5 kgIron 25 kgSand 100 kgGranulate 100 kgFinesFines 2020 kgkg
SAI
Output perOutput perton of waste:ton of waste:
Energy utilisation rate = 0,84Energy utilisation rate = 0,84EU discussion on R1/D10EU discussion on R1/D10
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Sorting After IncinerationSorting After Incineration
Sort
Bottom Bottom ashash
Cyclone
66--40mm40mm
22--6mm6mm
<2mm<2mm
Cleansand
Dewatering Sludge cakeSludge cake
Magnet Eddy current
Densityseparation
Magnet
IronNon-Femetals
Coarsegranulate
Finegranulate
Washing waterWashing water
ISWA
Bottomash treatmentplant
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HR-AVI project HR-AVI project
l Systematic approach to optimise recoveryl Using proven technologies in new combinationl Electrical efficiency >30%l New logistic concept
l Budget: 400 M€l Construction start: Begin 2004
l Completion: End 2006
l Systematic approach to optimise recoveryl Using proven technologies in new combinationl Electrical efficiency >30%l New logistic concept
l Budget: 400 M€l Construction start: Begin 2004
l Completion: End 2006
= WFPP= WFPP
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- Large 1st draw: Height >20m,Flue-gas velocity < 3m/s
- Large 2nd and 3rd-draw- Super-heater: Flue-gas velocity < 2,5 m/s- Second Economiser after fabric filter- Flue-gas recirculation
(primary and secondary air)
3e2e1e
Evaporator Superheater Economiser
2 3 4
terti
secu
terti
secu
Prim
1st 2nd850°C
3rd650°C
SSH1
180°C
1
4th
α
Ketelas 1 Ketelas 2
Bodemas
SSH2
SSH3
SSH4
ECO1
ECO2
ECO3
Sketch boiler designSketch boiler design
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Superheated steam 440-480°CSteam pressure 125-130 barSteam reheating after HP-turbineExtra economiser
Drum
Boiler
Reheater
25°C0,03 bar
Superheater
x12x
320°C13 bar
190°C14 bar
480°C130 bar
335°C135 bar
Turbine
Sketch steam reheatingSketch steam reheating
ISWA
GeneratorGenerator
Reheater (2x)Reheater (2x)
CondensorCondensor
Cooling waterCooling water
HP-TurbineHP-Turbine LP-TurbineLP-Turbine
Reheaters
ISWA
High Efficiency concept WFPP®
ISWA
Boiler WFPPBoiler WFPP
ISWA
Flue-gas cleaning WFPPFlue-gas cleaning WFPP
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Energy-potential in WasteEnergy-potential in Waste
Waste in EU: 182 MTon/year x 10 MJ/kg x 30%
Electricity: = 550 PJ / year= 150 TWh / year= 17.300 MW-continuous= 8 % of total EU-production
Avoided CO2 = 200 million tons per year
Waste in EU: 182 MTon/year x 10 MJ/kg x 30%
Electricity: = 550 PJ / year= 150 TWh / year= 17.300 MW-continuous= 8 % of total EU-production
Avoided CO2 = 200 million tons per year
ISWA
Efficiency breakdown
0%
20%
40%
60%
80%
100%
Conventional
Boiler losses(stack)Cooling =Loss20% el
0%
20%
40%
60%
80%
100%
WFPP
Boiler losses(stack)Cooling = Loss
30% el
20% el
0%
20%
40%
60%
80%
100%
Conv+ heat
Boiler losses (stack)
Cooling = Loss
Heat
20% el
Derating ofelectricity by heatdelivery
0%
20%
40%
60%
80%
100%
WFPP+ heat
Boiler losses(stack)
Cooling = Loss
Heat
30% el
20% el
Derating ofelectricity byheat delivery
Greenhouse effect overallGreenhouse effect overallGreenhouse effect overall
976 328 81 -153-349-173-219-15
-400
-200
0
200
400
600
800
1.000
DUMPSITE
LANDFILL
+ bioga
s eng
ines
WtE Ave
rage N
LWtE
Con
venti
onal
WtE O
ptimise
dWtE
Con
v.+CHP
WtE O
ptim.+CHP
WtE he
at on
ly
kg CO2/ton Waste
Landfill
Electricity Heat
Combined heat and power
Greenhouse gas balanceGreenhouse gas balance
-1500-1250-1000
-750-500-250
0250500750
100012501500[kg CO2 / ton Waste]
Avoided CO2 by Heat delivery 0 0 -25 0 0 -241 -210 -563Avoided CO2 by Electricity production 0 -33 -234 -332 -495 -248 -416 59Avoided CO2 by metal recovery 0 0 -44 -65 -98 -65 -98 -44Methane (CO2-equiv.) 1.251 693 15 15 15 15 15 15CO2 emission Fos.orig. 0 0 383 381 374 381 374 394CO2 emission Bio.orig. 208 151 468 468 468 468 468 468CO2 used for biomass -483 -483 -483 -483 -483 -483 -483 -483
DUMPSITE LANDFILL WtE
Average WtE Conv. WtE Optim.
WtE Conv.+CH
P
WtE Optim.+CH
P
WtE heat only
ISWA
WFPP® is the most cost-effective renewable option…
Sources: EZ, Regeling subsidiebedragen milieukwaliteit elektriciteitsproductie; VROM, personal communication;ECN, 2002, Duurzame Energie en Ruimte, M. Menkveld; analysis Deloitte
€
Cost per avoided ton CO2
0
20
40
60
80
100
120
140
Waste-2-Energy
WFPP®
Wind onland
Biomass Wind on sea Photo-voltaic
1033
€
Cost per avoided ton CO2
0
20
40
60
80
100
120
140
Waste-2-Energy
WFPP®
Wind onland
Biomass Wind on sea Photo-voltaic
1033€/ avoided
ton of CO
2€
/ avoidedton of C
O2
ISWA
Optimal Electrical efficiencyOPTIMISATION:•Local conditions
•Cooling water
•Type of waste
•Size of installation
•Electricity price
•Depreciation time
•Subsidies
•Environmental profile
•Permit conditions
OPTIMISATION:•Local conditions
•Cooling water
•Type of waste
•Size of installation
•Electricity price
•Depreciation time
•Subsidies
•Environmental profile
•Permit conditionsSource: W+G
05
101520253035
20 40 60 80 Electricity price [€/MWh]
Small installationBig installation
%%
ISWA
Income from waste and energy
110
0
10
20
30
40
50
60
-10 -5 0 5 10 15 20 25 30 35 40 45 50Year (before/after scheduled startup)
M€
/ yea
r
Extra lifetime 4th-generation
Gain on permitingHE
Green Fee
Aditional Electricity
Electricity
Waste
21
3 4
Business case for 4th-generation
ISWA
21
3 4Business case for 4th-generation
ISWA
Incineration
SYNERGYSYNERGY
Waste Water
Waste
Biogas Engines
Electricity
Water
ElectricitySewage Sludge
Biogas
Heat
Exhaust
Sewage Treatment
Plant
ISWA
Patents for licensingwith support for implementation
Flue gas Cleaning1. Dioxin removal in wet flue gas cleaning with detergents2. Mercury removal in wet flue gas cleaning3. Combining waste incineration and sewage treatment plant
Energy Recovery4. High Efficiency - Waste Fired Power Plant5. Flue gas recirculation to primary air6. Steam super heater construction with screen pipes7. Steam super heater with unround pipes
Material recovery8. Salt fabrication from flue gas cleaning residue9. Recovery of fine Non-Ferrous metals from bottom ash10. Gravity Separation of Non-Ferrous metals from bottom ash
Flue gas CleaningFlue gas Cleaning1.1. Dioxin removal in wet flue gas cleaning with detergentsDioxin removal in wet flue gas cleaning with detergents2.2. Mercury removal in wet flue gas cleaningMercury removal in wet flue gas cleaning3.3. Combining waste incineration and sewage treatment plantCombining waste incineration and sewage treatment plant
Energy RecoveryEnergy Recovery4.4. High Efficiency High Efficiency -- Waste Fired Power PlantWaste Fired Power Plant5.5. Flue gas recirculation to primary airFlue gas recirculation to primary air6.6. Steam super heater construction with screen pipesSteam super heater construction with screen pipes7.7. Steam super heater with Steam super heater with unroundunround pipespipes
Material recoveryMaterial recovery8.8. Salt fabrication from flue gas cleaning residueSalt fabrication from flue gas cleaning residue9.9. Recovery of fine NonRecovery of fine Non--Ferrous metals from bottom ashFerrous metals from bottom ash10.10. Gravity Separation of NonGravity Separation of Non--Ferrous metals from bottom ashFerrous metals from bottom ash
ISWA
6. CONCLUSION6. CONCLUSION
COST can/must go DOWN
SIMPLE process do it OPTIMAL
Environmental efficiency use all SYNERGY
Electrical Efficiency > 30%
COST can/must go DOWN
SIMPLE process do it OPTIMAL
Environmental efficiency use all SYNERGY
Electrical Efficiency > 30%
ISWA
Conclusion:
Waste is the directly available raw material for clean renewable energy and high quality building materials
Let’s explore together world’s most valuable mineral
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Tropical rain forestTropical rain forest
AEB Amsterdam
Picture WFPP