1. A Presentation on
TECHNO-ECONOMIC ANALYSIS OF AIR-BLOWN
INTEGRATED GASIFICATION COMBINED CYCLE (IGCC) POWER PLANT
WITH HYBRID CO2 CAPTURE SYSTEM
Sujit Karmakar
Department of Mechanical Engineering
National Institute of Technology Durgapur
West Bengal
Ajit Kumar Kolar
Heat Transfer and Thermal Power Lab
Department of Mechanical Engineering
Indian Institute of Technology Madras
Chennai, Tamil Nadu
Presented by
SUJIT KARMAKAR
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2. CONTENTS
 INTRODUCTION
 METHODOLOGY
 IGCC PLANT CONFIGURATION
 COAL CHARACTERISTICS
 PERFORMANCE PARAMETERS
 IGCC PLANT WITH HYBRID CO2 CAPTURE SYSTEM
 RESULT
 CONCLUSIONS
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3. INTRODUCTION
 Carbon dioxide (CO2) - key greenhouse gas (GHG)
causing global warming and affects climate adversely
World CO2 emission (2011) : 31 GT/yr
 India's
per capita per yr CO2 emission : 1.4 tonnes, less
than one-third of the world average and about 12 times
less than the United States
 India
accounts for about 5.5% of the world's CO2
emissions
(Source: IEA Key World Energy Statistics, 2011)
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4. INTRODUCTION
(CONTD..)
(Source: IPCC special report on CCS)
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5. INTRODUCTION
(CONTD..)
INTEGRATED GASIFICATION COMBINED CYCLE (IGCC)
ST
Steam
Coal
Gasifier
Hot gas
clean-up
Combustor
GT
HRSG
Air
Stack
• Elaborate gas clean-up (mainly consisting of particulate control) is required
before the gasifier product gas is combusted and sent to the gas turbine
(pre-combustion clean-up)
5
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6. METHODOLOGY
 3-E (energy, exergy, and environment) analysis is
carried out using a flow-sheeting program,
“Cycle-Tempo : Release 5 ”
 Simulation of MEA based CO2 capture plant using
flow sheet program “Aspen Plus: Release 2004”
 Economic analysis is carried out using annualized
and levelized costs of electricity generation
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7. IGCC POWER PLANT CONFIGURATION (BASE PLANT)
Single Pressure HRSG
Air Blown Gasifier
Gasifier operating Condition: 18 bar/950°C
Air/fuel: 1.58
Steam/fuel: 0.17
GT: 15.5 bar/1288°C
ST: 101 bar/540°C
CO2: 5-6 vol %
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8. COAL CHARACTERISTICS
Indian (High Ash - HA)
As-Received
Dry Basis
Proximate
Analysis
(wt%)
(wt%)
Fixed Carbon
24.00
27.27
Volatile Matter
21.00
23.86
Mineral Matter
43.00
48.87
Moisture
12.00
-
Ultimate
As-Received
Dry Basis
Analysis
(wt%)
(wt%)
Carbon
34.46
39.16
Hydrogen
2.43
2.76
6.97
7.92
Nitrogen
0.69
0.78
Sulfur
0.45
0.51
Mineral Matter
43.00
48.87
Moisture
12.00
-
HHV (MJ/kg)
13.96
15.83
Exergy (MJ/kg)
15.26
17.30
Oxygen
(by difference)
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9. PERFORMANCE PARAMETERS

Plant energy efficiency,
=

Net electricity output
Mass flow rate of coal HHV of the coal
Plant exergy efficiency,
Net electricity output
=
Mass flow rate of coal Specific exergy of the coal
Baehr correlation :
Ex coal
(0.9775 LHVcoal + 2.410)
(0.0065 LHVcoal + 0.054)
Excoal is specific exergy of coal in MJ/kg
 Levelized cost of electricity (LCoE)
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10. IGCC POWER PLANT WITH HYBRID CO2 CAPTURE SYSTEM
WGS Reaction: CO + H2O ↔ CO2 + H2
CO2 concentration: 11 vol %
HT WGS: 400°C
LT WGS: 210°C
CO2 selective rubbery
polymeric membranepermeance 1000 GPU
Two-stage membrane
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11. MEA BASED CO2 CAPTURE SYSTEM
Absorber stages: 10
Reboiler heat duty: 238 MWth
Stripper stages: 12
(4.3 MJ/kg of CO2)
Lean MEA loading: 0.2
Aqueous MEA solution: 30% vol.
Absorber operating pressure: 1.2 bar
Stripper operating pressure: 1.9 bar
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12. RESULT-PERFORMANCE
HYBRID CO2 CAPTURE
Power output (MWe)
Gas turbine
Without CO2 capture
With CO2 capture
286
286
Steam turbine
171
140
Total
Plant energy efficiency (%)
457
37.9
426
26.2
Plant exergy efficiency (%)
34.8
24.0
MEA BASED CO2 CAPTURE
Plant energy efficiency (%)
37.9
24.3
Plant exergy efficiency (%)
34.8
22.3
MEMBRANE BASED CO2 CAPTURE
Plant energy efficiency (%)
37.9
24.1
Plant exergy efficiency (%)
34.8
22.1
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13. RESULT-PERFORMANCE
Energy Balance- IGCC Pant without/ with CO2 capture
Component
Power (efficiency)
Heat rejected in cooling water
Heat rejected through stack
Heat rejected in bottom ash
CO2 capture
Others
Without CO2 capture
37.9
27.6
22.1
8.3
4.1
With CO2 capture
26.2
10.1
7.6
8.3
43.3
4.5
Energy Balance- MEA based CO2 capture plant
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14. RESULT-PERFORMANCE
Exergy Balance- IGCC Pant
Component
Power (efficiency)
Loss in gasifier
Loss in combustor
Loss in bottom ash
Loss in HRSG
Loss through stack
Loss in steam turbine
Loss in gas turbine
Loss in condenser and cooling water
Loss due to CO2 capture
Others
Without CO2 capture Without CO2 capture
34.8
24.0
18.4
18.4
14.9
15.6
7.4
8.1
5.0
5.1
4.9
1.1
2.6
1.9
2.1
2.0
1.1
0.4
12.9
8.8
10.5
Economic Analysis- IGCC Pant without/ with CO2 capture
Without CO2 capture
LCoE (INR/kWh)
3.33
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With CO2 capture
5.21
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15. CONCLUSIONS
 The plant energy and exergy efficiencies are about 37.9 and 34.8%,
respectively for the IGCC plant without CO2 capture whereas, the same
are 26.2 and 24%, respectively with CO2 capture and about 11.7%-points
of plant energy efficiency is dropped due to CO2 capture.
 Majority of energy loss takes place during CO2 capture and the loss in
reboiler is found maximum, contributing 45% of the total losses during
CO2 capture.
 The reboiler heat duty in the MEA based CO2 capture system is 238 MWth
which is equivalent to 4.3 MJ per kg of CO2 captured.
 Maximum exergy destruction is in the gasifier which contributes 18.4% for
the IGCC plant without or with CO2 capture.
 The levelized cost of electricity generation of an IGCC plant without and
with hybrid CO2 capture system is estimated approx. INR 3.33 and 5.91
per kWh, respectively.
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16. REFERENCES
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17. Thank You
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