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Update on Work Package 3 CO2 capture

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Title: Update on Work Package 3 CO2 capture


1

Update on Work Package 3 CO2 capture Presented
by Jon Gibbins 23 October, 2008
2
Work Package 3 (WP3) Case studies for CO2
Capture Partners GreenGen (GG) Institute of
Engineering Thermophysics, Chinese Academy of
Science (IET) State Key Laboratory of Chemical
Engineering, Tsinghua University (DCE) Department
of Thermal Engineering, Tsinghua University
(DTE) BP Clean Energy Research Education
Centre, Tsinghua University (THCEC) Thermal
Power Research Institute (TPRI) North China
Electric Power University (NCEPU) Wuhan
University (WHU) Zhejiang University
(ZJU) Imperial College (Imp) Alstom Power
(Alstom) BP (BP) Univ. of Cambridge Doosan
Babcock (DB) Shell (Shell)
3
  • Description of tasks in WP3
  • Task 1 Initial Phase Definition of basic
    conditions and reference basis
  • Completed in August 2008.
  • Typical Chinese site, Shenhua and Datong coals
  • Task 2 Case Studies (similar scope to IEA GHG
    studies)
  • Subtask 2.1 Oxyfuel
  • OX1 Oxyfuel, new build Capture-Ready, (Doosan
    Babcock ZJU)
  • b) OX2 Oxyfuel, capture retrofit to existing
    sub-critical plant combined with ASCBTR,
    (Doosan-Babcock)
  • Now in progress.
  • 800MW, superheater steam temperature 600ºC
  • 350MW existing Chinese plants, will be upgraded
    to supercritical steam conditions and oxyfuel
    capture with essentially no loss in efficiency

4
Subtask 2.2 Post-combustion
Houshi Power Plant 600 MW supercritical Steam
pressure 266 bar Superheater steam temperature
540.6 ºC
a) PC1 Post-combustion capture, new build,
(Alstom DCE) b) PC2 Post-combustion capture,
capture-ready, and retrofit (Alstom DTE) c)
PC3 Super-critical with post-combustion capture
by chemical absorption and membrane contactor
(ZJU) d) PC4 Possible post-combustion capture
options for existing sub-critical and
supercritical power plants (i.e. Chinese power
plant fleet in 10-20 years time) (NCEPU)
  • 600 MW supercritical sliding pressure PC boiler

5
Subtask 2.3 Pre-combustion based on
gasification a) GS1 IGCC pre-combustion
capture, Chinese gasifier, (GG TPRI) b) GS2
Polygeneration pre-combustion capture,
BP-Tsinghua c) GS3 IGCC pre-combustion
capture, Shell gasifier d) GS4 Polygeneration
pre-combustion capture, Shell gasifier,
(ShellIET)
SCGP based IGCC at Nuon Buggenum 2000 t/d
coal 253 MWe
6
Generic GT characteristics for IGCC with
capture Performance on methane
GT Power MW 256 ST Power MW 118 Net
Power MW 374 Net Cycle Efficiency 53 Fuel
Type Nat Gas Inlet Flow (W) kg/sec 830 Pre
ssure Ratio 17 Burner Exit Temp K 1550 TRIT
K 1500 Turbine Exit Temp K 791 Rotational
Speed (N) RPM 3000
7
Subtask 2.4 Case study suitable for specific
conditions of China Coal based polygeneration
systems integrating pre-combustion capture and
alternative fuel (MeOH or DME) production,
including liquid fuel transport from western
China via pipeline for use in power plants.
(IETZJU) Task 3 Transportation
technologies Wuhan and Shell collaborating on
pipeline models for China. Will be specifying
typical Chinese plant-to-storage pipeline routes
shortly to assess pipeline design and indicative
costs. Task 4 Comparison of case studies and
key technologies to be developed in the next
phase GreenGen pre-feasibility study in progress,
other sub-tasks to start in New Year
8
Conclusions Work Package progressing on time Good
exchange of information between Chinese and UK
partners Number of collaborative activities
planned before next meeting in early 2009 Interim
report at end of November 2008.
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