MBX-102/JNJ39659100, a Novel Peroxisome Proliferator-Activated ...
Dynamic Simulation Study on IGCC Process with Novel Activated Carbon ... 8B and 9B/9B1 Yu… ·...
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Dynamic Simulation Study on IGCC Process with Novel
Activated Carbon based Pre-combustion Carbon Capture
10th ECCRIA Conference (UoH)
Authors: Y. Wang1, S. Caldwell2, *J. Wang1, J. Wood2, S. Guo1
1School of Engineering, University of Warwick, UK
2School of Chemical Engineering, University of Birmingham, UK
17th Sep 2014
Power and Control Systems Research Laboratory
School of Engineering
University of Warwick
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Content • Overview of the project
• Project introduction
- ASU unit
- Gasifier module: raw syngas
- WGS module: shifted syngas
- Combined cycle and power generation
- Energy analysis of IGCC with/without CC unit
• Summary
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Overview of the project
• General acceptance that CO2 emissions are affecting the
climate
• UK emissions targets for power stations is a reduction from
500 to 50 gCO2/kWhr by 2030 (1)
• Up to 18 GW of investment of CCS power stations is
possible in the 2020s
• By 2030, 26% of global emissions from China, with 98% of
power generation emissions from coal (2)
• $2.7 trillion investment in power by 2030 (3)
• 50/50 split favouring pre-combustion to post-combustion
capture (3) 1. Turner, A. et al. The Fourth Carbon Budget - Reducing emissions through the 2020s. London :
Committee on Climate Change, 2010.
2. Grubb, M. Generating Electricity in a Carbon Constrained World. London : Elsevier, 2010.
3. Liang, X et al. 2011, Applied Energy, Vol. 88, pp. 1873-1885
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Overview of the project • Collaboration between Nottingham, Birmingham, Warwick, UCL,
Institute of Coal Chemistry (Chinese Academy of Sciences) and
Tsinghua University (China)
• Project looks to investigate the next generation of Activated Carbon
adsorbents for CO2 capture in IGCC processes
• Project Split into 2 tasks
– Active Carbon preparation, characterisation, testing and modelling
– Modelling the impact of CO2 capture on the operation of IGCC
processes
• The role of Warwick:
– To develop a complete process of IGCC power plant model integrated
with pre-combustion carbon capture process.
– To conduct simulation study and analysis of dynamic responses of the
whole plant.
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Overview of the project
Key modules for IGCC process:
a.GEM with auxiliary systems:Coal feed, ASU, Gasifier, WGS;
b.Combined cycle system: Gas turbine, Heat recovery boiler, steam turbine.
Figure1. Simplified ‘capture ready’ IGCC power plant procedure
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Content • Overview of the project
• Project introduction
- ASU unit
- Gasifier module: raw syngas
- WGS module: shifted syngas
- Combined cycle and power generation
- Energy analysis of IGCC without CC unit
• Summary
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Project introduction- ASU
Figure1. Simplified ‘capture-ready’ IGCC power plant procedure
Stream Air O2 HP N2 MP N2
LP N2
F 1 0.21 0.066 0.262 0.459
X N2 0.781 0.017 1 0.991 0.982
X O2 0.21 0.95 0 0.002 0.004
X Ar 0.009 0.033 0 0.007 0.014
P bar 5.07 48 88 25 1.15
T 293 295 295 500 295
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Air separation unit (distillation process)
Coal type Illinois 6 Australia Fluid Coke
Specific energy
consumption KJ/mol air 4.76 4.76 4.76
Total energy
consumption MW 17.7 17.9 21.2
Feed pre-processing
MW 8.3 8.4 10.0
MHX MW 3.0 3.0 3.5
Distillation MW 4.7 4.7 5.6
Post processing MW 1.7 1.8 2.1
Table 1: Break-down of the total energy destruction over the different process parts of the
two-column ASU design.
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Content • Overview of the project
• Project introduction
- ASU unit
- Gasifier module: raw syngas
- WGS module: shifted syngas
- Combined cycle and power generation
- Energy analysis of IGCC without CC unit
• Summary
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Project introduction- Gasifier
Figure1. Simplified ‘capture-ready’ IGCC power plant procedure
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Project introduction- Gasifier
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Gasifier module
Gasifier model input Comparison of simulation
result and reference data
Used for the raw syngas
input to the following
modules
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Gasifier module steady state analysis
Figure6.Syngas content change with coal slurry
concentration unit(kg/kg)
Figure7. Syngas content change with coal slurry concentration
unit (kg/kg)
Figure8. Syngas content change with oxygen/coal
ratio unit(kg/kg)
Figure 9. Syngas content change with oxygen/coal
ratio(kg/kg)
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Three different type of coal are applied to the simulation to test the process
dynamic response. The syngas flow rises from 0.1 to 100mol/s within 100
seconds and it will first enter the WGS module for shift reaction.
Gasifier module generate raw syngas
Figure 10. Analysis of Texaco gasifier (quench)
Ilinois6 Australia Fluid Coke
Coal input (t/h) 100 100 100
Dry feed stock thermal energy input -
LHV(MW) 817.89 770.64 824,77
Oxygen input (t/h) 86 87 103
Syngas generation (kmol/s) 3.1 3.1 3.2
Carbon conversion rate(%) 98 98 98
Cold gas efficiency (%) 71.5 70.0 74.2
Raw syngas H2 mol% 30.1 29.6 23.7
Raw syngas CO mol% 41 35.4 47.2
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Content • Overview of the project
• Progress introduction
- ASU unit
- Gasifier module: raw syngas
- WGS module: shifted syngas
- Combined cycle and power generation
- Energy analysis of IGCC without CC unit
• Summary
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Project introduction- GEM
Raw syngas contains H2, CO, CO2, CH4, H2O, N2,O2
WGS reaction:
Built with Simulink-based toolbox- Thermolib:
Calculation of syngas content
change and heat recovery
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Water gas shift reactor module
Figure 11. Shifted syngas CO2
concentration dynamic change
Figure 12. Shifted syngas H2
concentration dynamic change
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Water gas shift reactor module
Figure 13. Shifted syngas temperature dynamic change
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Content • Overview of the project
• Project introduction
- ASU unit
- Gasifier module: raw syngas
- WGS module: shifted syngas
- Combined cycle and power generation
- Energy analysis of IGCC without CC unit
• Summary
• Future work
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Gas turbine module Brayton cycle
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Gas turbine with HRSG
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Project introduction- Combined Cycle
Fig5 . Gas turbine power
output dynamic change
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Combined cycle module
Figure 14. Gas turbine power output dynamic change
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Combined cycle module
Figure 15. Combined cycle power output dynamic change
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Content • Overview of the project
• Project introduction
- ASU unit
- Gasifier module: raw syngas
- WGS module: shifted syngas
- Combined cycle and power generation
- Energy analysis of IGCC with/without CC unit
• Summary
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Energy analysis of IGCC without CC unit Ilinois6 Australia Fluid Coke
Gross electricity efficiency (%) 45.2 45.3 45.2
Net power efficiency (%) 41.7 43.8 43.6
Coal input (t/h) 100 100 100
Dry feed stock thermal energy input -
LHV(MW) 817.89 770.64 824,77
Oxygen input (t/h) 86 87 103
Syngas generation (kmol/s) 3.1 3.1 3.2
Cold gas efficiency (%) 71.5 70.0 74.2
Carbon conversion rate(%) 98 98 98
Gas turbine output (MW) 238.2 220.2 236.4
Steam turbine output (MW) 158.8 146.8 157.6
Combined cycle output (MW) 370 367 394
ASU power consumption+O2
compression (MW)
19.35 19.575 23.175
Total ancillary power
consumption
28.88 29.22 34.59
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Energy analysis of IGCC with CC unit
Power consumption:
Pressurization; H2 loss along with CO2 capture;
Fig 16. Experiment bed in UoB
Reference: Calin-Cristian Cormos, Integrated assessment of IGCC power generation technology with carbon capture and storage (CCS), Energy, Volume
42, Issue 1, June 2012, Pages 434-445, ISSN 0360-5442, http://dx.doi.org/10.1016/j.energy.2012.03.025.
(http://www.sciencedirect.com/science/article/pii/S0360544212002162) Keywords: Power generation; IGCC; CCS (Carbon capture and storage); Techno-
economic and environmental evaluations
1. Pressurization;
2. Adsorption;
3. Depressurization
& pressurization;
4. Blow down;
5. Purge(rinse)
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Energy analysis of IGCC without CC unit
Heavy product: CO2 stream
Light product: sweet syngas
Ilinois6 Australia Fluid Coke
Shifted syngas H2 mol% 57.6 56.8 53.2
Shifted syngas CO2 mol% 41.1 42.0 45.3
Sweet syngas CO2 mol% 3.27 3.35 3.61
Sweet syngas H2 mol% 50.2 49.51 46.34
Gross efficiency loss%
(92% CO2 captured) 12.8 12.8 12.8
Reference efficiency loss%
(93% CO2 captured post-combustion) 8.78 8.78 8.78
92% CO2 captured
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Energy analysis of IGCC without CC unit
Heavy product: CO2 stream
Light product: sweet syngas
Ilinois6 Australia Fluid Coke
Shifted syngas H2 mol% 57.6 56.8 53.2
Shifted syngas CO2 mol% 41.1 42.0 45.3
Sweet syngas CO2 mol% 3.27 3.35 3.61
Sweet syngas H2 mol% 50.2 49.51 46.34
Gross efficiency loss%
(80% captured) 6.5 6.5 6.5
Reference efficiency loss%(93.98%
captured post-combustion) 8.78 8.78 8.78
80% CO2 captured
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Content • Overview of the project
• Progress review
- ASU unit
- Gasifier module: raw syngas
- WGS module: shifted syngas
- Combined cycle and power generation
- Energy analysis of IGCC with/without CC unit
• Summary
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Summary • For air separation unit, the pre-processing of air accounts for 47% of total
energy consumption while the distillation process takes 26.5%, the transport
of liquefied oxygen and nitrogen will cause further loss;
• Rise of coal slurry concentration will improve the syngas quality while the
oxygen input need to controlled carefully;
• The integration of individual ASU and IGCC is important for energy saving
and efficiency improvement;
• The main reason of energy loss cased by CO2 capture is the H2 loss, in terms
of carbon capture rate higher than 90%, PSA consume relative more energy
than post-combustion capture process;
• Shifted syngas can be used to heat the steam of HRSG, and cooled shifted
syngas will be ready for carbon capture process;
• Model in Matlab and Simulink environment can successfully reflect the whole
picture of IGCC dynamic system;
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THANKS FOR
YOUR ATTENTION!