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Comparison Between Landfill Gas and
Waste Incineration for Power
Generation in Accra, Ghana
Serwaa ANAGLATE
Syawalianto RAHMAPUTRO
Carlos RUIZ

Prof. Luis Rojas

1
Outline
 Accra
 Objective & Scope

 RETScreen
 Waste Characterization
 Landfill Gas
 Waste Incineration

 Results
 Social Impact
 Conclusions
 Outlook

2
Accra, Ghana

 1,800 Daily Tons of Waste
 Open Dump Sites

 Insufficient Waste Collection
 Insufficient Power Capacity

Source: www.atokd.com

Source: http://raklak.wordpress.com

3
Objective & Scope
Objective
 Assess and compare landfill gas and waste incineration
 Technical
 Environmental
 Economic
 Social Impact

Scope
 Total Electricity Exported
 GHG Emissions Reduction
 Approximate Costs
 Financial Summary
 Pre-feasibility Level
4
RETScreen®

 Free Software
 Clean Energy Project Analysis
 Inexpensive Technical and Financial Feasibility Analysis

Energy
Model

Cost
Analysis

GHG
Analysis

Financial
Summary

Sensitivity
& Risk
Analysis

5
Waste Characterization
3%

3%

3%

2%

6%

17%
66%

Organic

Inert

Paper

Plastic

Glass

Metal

Textile & Leather
6
Landfill Gas

Source: Affiliated Engineers, 2010

7
Landfill Gas Simulation
Amount of
Waste

Input Parameter

Value

Waste Disposal Rate (mi)

270,000 t/yr

Landfill Opening Year

2014

Landfill Closing Year

2044

Generation Constant (k)

0.06 yr-1

Generation Potential (Lo)

Waste
Composition

170 m3/t

Climatic
Conditions

6MW
 Assumptions:
 Constant Biodegradable Fraction in
Waste

 50% of CH4 by Volume
 75% Collection Efficiency
8
Waste Incineration
Electricity
Generation

 Pretreatment  Furnace -

Waste
Incinerator

Flue Gas
Treatment

Drying in the receiving pit.

Source: www.sick.com

Moving grate furnace is the most

Boiler

robust.

 Energy Recovery - Low-pressure steam

boiler is convenient when energy recovery is designed for
electricity use only (Haukohl, J., Rand, T., & Marxen, R.
,1999)

 Energy Production -

Rankine cycle with
steam turbine, condenser, boiler, and pump for power
generation.

 Flue Gas Treatment -

For 600 ton to 900
ton/day: SNCR, semi-dry scrubber, activated carbon, and
a bag house filter are usually used
(Kuo, Lin, Chen, Tseng, & Wey, 2011).

Grate
Furnace

Receiving Area
Receiving Pit

Source: www.valorena.fr

9
Waste Incineration Simulation
Proximate AnalysisAsh
Combustibles Moisture
14%
Ash

31%

1

Waste
Analysis

WASTE INCINERATION
Waste Feed Rate
Dry Weight of
Feed Waste

270,000
120,727.12

Feeding Rate
Lower Heating
Value

Moisture

55%
t/yr
t/yr

13.78

t/hr

15.854

Ultimate Analysis

2

Fuel
Potential

POWER SYSTEM

GJ/t

Fuel Potential 218.49 Gj/hr

Predefined:
• Udomsri, Petrov, Martin, &
Fransson, 2011
• Suggested values from RETScreen

Simulation:
Energy Model

Combustibles

3

Power
Generation

Availability

8,401

hours

Back
Pressure

5.6

kPa

Steam
Temp.

380

°C

Return
Temp.

90

°C

Steam Flow

68,600

kg/hr

Operating
Pressure

80

bar

Turbine
Efficiency

75

%

Fuel Required 218 Gj/hr

10
Results – Energy and Environment
Landfill
Gas

Technology
Engine Power Capacity
(kW)
Electricity Exported
(MWh/yr)

Waste
Incineration

6,000

16,505.24

48,000 138,658

Electricity Export Rate - $ 58.7
Source:
www.engineeringnews
.co.za

Source:
www.siemenspowergeneration.c
om

Technology
Landfill Gas
Waste Incineration

Emission Factor (Kg/GJ)
CO2

CH4

N 2O

Annual GHG
Reduction (tCO2)

0

0.0040

0.00010

273,657

29.43

0

0.00315

41,413.4

Energy Mix in Ghana:
• Hydro Power 67.6%
• Thermal Power 32.4%

 WI energy output > 8 times that of LFG
 GHG reductions are achieved in both technologies
 LFG GHG reductions > 6 times that of WI
11
Results - Financial
25,000,000
Cost Breakdown

Accumulated
Landfill Gas
WI

CashFinancial
Flow

20,000,000
Cash Flow (USD)

Engineering

$ 3,743,026

$ 10,455,025

$ 7,512,749

Balance of System

$ 3,630,152

$ 23,679,131

Total Initial Cost

$ 15,135,177

$ 34,934,905

5,000,000

Results

8.1%

4.8%

Payback Period

$ 1,050,000

Power System
10,000,000

WI

IRR

Initial Cost

15,000,000

Landfill Gas

13.2

15.9 years

Annual Income

$2,817,600

$8,139,215

Net Present Value
(NPV)
Benefit-Cost Ratio

$4,612,086

$826,358

1.61

1.05

Project Year

0

1 2 3
Annual Cost 0
-5,000,000 and Debt
Payment

4

5

6

7

8

9

10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25

-10,000,000
O&M

$ 1,531,000

$ 5,460,225

Debt Payment (10 yr)

$ 1,028,193

$ 2,373,267

$ 2,559,193

$ 7,833,492

$ 2,817,600

$ 8,139,215

-15,000,000

Total Annual Cost

LFG

Waste Incineration

-20,000,000
Annual Income

 Inflation Rate – 3%

 Debt Interest Rate – 6%

 Discount Gas rendered better profitability
 Electricity Export Escalation – 2%
 Landfill Rate – 4.5%
 Since Ghana is a developing country, affordability is important
12
Social Impact

 Job Creation

Source: www.rvg-ghana.com

 Improvement of the City’s Image
 Improved Sanitation
Source: Schah Fekri, 2011

 Productivity Increase

Source: Journalists for Human Rights, 2010

13
Conclusion & Outlook
 Both technologies are environmentally friendly and
economically feasible.
 Any solution would represent a great improvement.
 LFG is preferred due to its outstanding environmental
performance.
 WI is more suitable in case of limited space.
 Risk and sensitivity analysis are recommended.
 Inclusion of carbon credits should be considered.
 Further on-site tests should be carried out.
14
Thank you.
Any Questions?

Pictures in cover page courtesy of:
•www.treehugger.com
•Graham Turner (http://www.guardian.co.uk)
•www.sick.com

15

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Waste to Energy Project in Ghana: Landfill Gas or Incineration

  • 1. Comparison Between Landfill Gas and Waste Incineration for Power Generation in Accra, Ghana Serwaa ANAGLATE Syawalianto RAHMAPUTRO Carlos RUIZ Prof. Luis Rojas 1
  • 2. Outline  Accra  Objective & Scope  RETScreen  Waste Characterization  Landfill Gas  Waste Incineration  Results  Social Impact  Conclusions  Outlook 2
  • 3. Accra, Ghana  1,800 Daily Tons of Waste  Open Dump Sites  Insufficient Waste Collection  Insufficient Power Capacity Source: www.atokd.com Source: http://raklak.wordpress.com 3
  • 4. Objective & Scope Objective  Assess and compare landfill gas and waste incineration  Technical  Environmental  Economic  Social Impact Scope  Total Electricity Exported  GHG Emissions Reduction  Approximate Costs  Financial Summary  Pre-feasibility Level 4
  • 5. RETScreen®  Free Software  Clean Energy Project Analysis  Inexpensive Technical and Financial Feasibility Analysis Energy Model Cost Analysis GHG Analysis Financial Summary Sensitivity & Risk Analysis 5
  • 8. Landfill Gas Simulation Amount of Waste Input Parameter Value Waste Disposal Rate (mi) 270,000 t/yr Landfill Opening Year 2014 Landfill Closing Year 2044 Generation Constant (k) 0.06 yr-1 Generation Potential (Lo) Waste Composition 170 m3/t Climatic Conditions 6MW  Assumptions:  Constant Biodegradable Fraction in Waste  50% of CH4 by Volume  75% Collection Efficiency 8
  • 9. Waste Incineration Electricity Generation  Pretreatment  Furnace - Waste Incinerator Flue Gas Treatment Drying in the receiving pit. Source: www.sick.com Moving grate furnace is the most Boiler robust.  Energy Recovery - Low-pressure steam boiler is convenient when energy recovery is designed for electricity use only (Haukohl, J., Rand, T., & Marxen, R. ,1999)  Energy Production - Rankine cycle with steam turbine, condenser, boiler, and pump for power generation.  Flue Gas Treatment - For 600 ton to 900 ton/day: SNCR, semi-dry scrubber, activated carbon, and a bag house filter are usually used (Kuo, Lin, Chen, Tseng, & Wey, 2011). Grate Furnace Receiving Area Receiving Pit Source: www.valorena.fr 9
  • 10. Waste Incineration Simulation Proximate AnalysisAsh Combustibles Moisture 14% Ash 31% 1 Waste Analysis WASTE INCINERATION Waste Feed Rate Dry Weight of Feed Waste 270,000 120,727.12 Feeding Rate Lower Heating Value Moisture 55% t/yr t/yr 13.78 t/hr 15.854 Ultimate Analysis 2 Fuel Potential POWER SYSTEM GJ/t Fuel Potential 218.49 Gj/hr Predefined: • Udomsri, Petrov, Martin, & Fransson, 2011 • Suggested values from RETScreen Simulation: Energy Model Combustibles 3 Power Generation Availability 8,401 hours Back Pressure 5.6 kPa Steam Temp. 380 °C Return Temp. 90 °C Steam Flow 68,600 kg/hr Operating Pressure 80 bar Turbine Efficiency 75 % Fuel Required 218 Gj/hr 10
  • 11. Results – Energy and Environment Landfill Gas Technology Engine Power Capacity (kW) Electricity Exported (MWh/yr) Waste Incineration 6,000 16,505.24 48,000 138,658 Electricity Export Rate - $ 58.7 Source: www.engineeringnews .co.za Source: www.siemenspowergeneration.c om Technology Landfill Gas Waste Incineration Emission Factor (Kg/GJ) CO2 CH4 N 2O Annual GHG Reduction (tCO2) 0 0.0040 0.00010 273,657 29.43 0 0.00315 41,413.4 Energy Mix in Ghana: • Hydro Power 67.6% • Thermal Power 32.4%  WI energy output > 8 times that of LFG  GHG reductions are achieved in both technologies  LFG GHG reductions > 6 times that of WI 11
  • 12. Results - Financial 25,000,000 Cost Breakdown Accumulated Landfill Gas WI CashFinancial Flow 20,000,000 Cash Flow (USD) Engineering $ 3,743,026 $ 10,455,025 $ 7,512,749 Balance of System $ 3,630,152 $ 23,679,131 Total Initial Cost $ 15,135,177 $ 34,934,905 5,000,000 Results 8.1% 4.8% Payback Period $ 1,050,000 Power System 10,000,000 WI IRR Initial Cost 15,000,000 Landfill Gas 13.2 15.9 years Annual Income $2,817,600 $8,139,215 Net Present Value (NPV) Benefit-Cost Ratio $4,612,086 $826,358 1.61 1.05 Project Year 0 1 2 3 Annual Cost 0 -5,000,000 and Debt Payment 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 -10,000,000 O&M $ 1,531,000 $ 5,460,225 Debt Payment (10 yr) $ 1,028,193 $ 2,373,267 $ 2,559,193 $ 7,833,492 $ 2,817,600 $ 8,139,215 -15,000,000 Total Annual Cost LFG Waste Incineration -20,000,000 Annual Income  Inflation Rate – 3%  Debt Interest Rate – 6%  Discount Gas rendered better profitability  Electricity Export Escalation – 2%  Landfill Rate – 4.5%  Since Ghana is a developing country, affordability is important 12
  • 13. Social Impact  Job Creation Source: www.rvg-ghana.com  Improvement of the City’s Image  Improved Sanitation Source: Schah Fekri, 2011  Productivity Increase Source: Journalists for Human Rights, 2010 13
  • 14. Conclusion & Outlook  Both technologies are environmentally friendly and economically feasible.  Any solution would represent a great improvement.  LFG is preferred due to its outstanding environmental performance.  WI is more suitable in case of limited space.  Risk and sensitivity analysis are recommended.  Inclusion of carbon credits should be considered.  Further on-site tests should be carried out. 14
  • 15. Thank you. Any Questions? Pictures in cover page courtesy of: •www.treehugger.com •Graham Turner (http://www.guardian.co.uk) •www.sick.com 15