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CO2 Compression and Transport
Ron Munson and Neil Wildgust
Global CCS Institute
INTRODUCTION TO CAPTURE, USE AND GEOLOGICAL STORAGE OF CO2
January 22-23 2015
University of Sonora, Hermosillo
SUPPORTED BY:
Review of the Process – Post-Combustion
SUPPORTED BY:
PC Boiler
(With SCR)
Sulfur
Removal
Particulate
Removal
Ash
Coal
STEAM
CYCLE
CO2 Capture
Process*
ID Fan
Air
Power
CO2
Comp.
Flue Gas
CO2 To Storage
2,215 psia
Low Pressure Steam
Optional Bypass
(<90% Capture)
Review of the Process – Pre-Combustion
SUPPORTED BY:
Gasifier
&
Quench
Particulate
Removal
Slag
Coal
Steam
Turbine
CO2
Capture
Steam
Heat
Recovery
Air
Separation
Water
O2
N2Air
Water
Gas Shift
H2S
Removal
Steam
Sulfur
Recovery
Sulfur
Combustion
Turbine
Heat
Recovery
Air
Electric
Power
Flue Gas
Electric
Power
Fuel Gas
Steam
POWER BLOCK
CO2
Conditioning
Fuel Gas
Conditioning
w/reheatH2O / N2
CO2 to
StorageVent
Syngas
Cooling
Water
Why Do We Need to Compress the CO2?
SUPPORTED BY:
• Volume Reduction
Transport
 Reduce size of pipelines – lower capital cost
Storage
 Drops out water
 Reduces need for pore space
CO2 Compression and Purity Requirements
SUPPORTED BY:
• Compressed to 2200 psi for transport and storage
• Minimum 95% CO2 content
Impact of Compression on CCS Cost
SUPPORTED BY:
*No Capture Base = 64 mills/kWh
*90% CO2 Capture
*Compression to 2,200 Psia
*50 Mile Pipeline + Saline Formation Storage + 100 Years Monitoring
0
10
20
30
40
50
60
70
80
90
PercentIncreaseinCOE
Trans., Stor., & Monit.
Compression Capital
Capture Capital
Capture Operating
Capture Steam
Capture Aux. Power
Compression power
2%
Parasitic Power
h COE by 52%
Operating Cost
h COE by 7%
Capital Cost
h COE by 27%
Centrifugal Compression
SUPPORTED BY:
• High volume flows
• Unique
characteristics of CO2
for compressor
design
Real gas effects
High volume
reduction
Low speed of sound
Avoiding liquid
formation
Beam-Style Compressors
SUPPORTED BY:
• Commonly used in
petrochemical and natural
gas industries
• Straight through or back-to-
back configurations
• Intercooling between 2
sections and/or between
units
• High reliability – minimal bearings/seals
• High pressure – up to 15,000 psi
Internally-geared Compressors
SUPPORTED BY:
• Electric motor drives large
bull gear that drives multiple
pinion gears with centrifugal
compressors on each end
• Gear speeds increase with
pressure
• Separate inlet and outlet
flanges permit intercooling at
each stage
• Potential reliability issues – many bearings, seals,
and unshrouded impellers
Why interest in isothermal compression?
SUPPORTED BY:
Innovations in Compressor Design
SUPPORTED BY:
• Internally-cooled
compressor
stage
Performance of
internally-geared
compressor
Reliability of
beam-style
compressor
Reduced overall
footprint
─ Red - CO2 flow
path through
compressor stage
─ Blue - Liquid
cooling in the
diaphragm
─ Grey - Solid
Innovations in Compressor Design
SUPPORTED BY:
• Supersonic shock
wave compression
1/10th the physical
size
40 – 50% of the
installed capital cost
Heat integration to
offset energy penalty
10:1 compression
ratio
2-stage system
Pipeline Transport Systems
SUPPORTED BY:
Pipeline Costs
SUPPORTED BY:
Ship Transport
SUPPORTED BY:
CO2 Transport Hazards
SUPPORTED BY:
•Low temperature releases
•High pressures
•Corrosion
•High vapour density
•Detection issues
CO2 Transport Hazards
• CO2 can be tolerated in
quite high
concentrations without
permanent risk to
health
• BUT if those exposed
have key tasks to
execute their response
may be impaired
• THUS need to consider
effects during
emergency situations
SUPPORTED BY:
Pipeline Depressurization
SUPPORTED BY:
Thank you!
INTRODUCTION TO CAPTURE, USE AND GEOLOGICAL STORAGE OF CO2
January 22-23 2015
University of Sonora, Hermosillo
SUPPORTED BY:

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Overview on compression and transport of CO2

  • 1. CO2 Compression and Transport Ron Munson and Neil Wildgust Global CCS Institute INTRODUCTION TO CAPTURE, USE AND GEOLOGICAL STORAGE OF CO2 January 22-23 2015 University of Sonora, Hermosillo SUPPORTED BY:
  • 2. Review of the Process – Post-Combustion SUPPORTED BY: PC Boiler (With SCR) Sulfur Removal Particulate Removal Ash Coal STEAM CYCLE CO2 Capture Process* ID Fan Air Power CO2 Comp. Flue Gas CO2 To Storage 2,215 psia Low Pressure Steam Optional Bypass (<90% Capture)
  • 3. Review of the Process – Pre-Combustion SUPPORTED BY: Gasifier & Quench Particulate Removal Slag Coal Steam Turbine CO2 Capture Steam Heat Recovery Air Separation Water O2 N2Air Water Gas Shift H2S Removal Steam Sulfur Recovery Sulfur Combustion Turbine Heat Recovery Air Electric Power Flue Gas Electric Power Fuel Gas Steam POWER BLOCK CO2 Conditioning Fuel Gas Conditioning w/reheatH2O / N2 CO2 to StorageVent Syngas Cooling Water
  • 4. Why Do We Need to Compress the CO2? SUPPORTED BY: • Volume Reduction Transport  Reduce size of pipelines – lower capital cost Storage  Drops out water  Reduces need for pore space
  • 5. CO2 Compression and Purity Requirements SUPPORTED BY: • Compressed to 2200 psi for transport and storage • Minimum 95% CO2 content
  • 6. Impact of Compression on CCS Cost SUPPORTED BY: *No Capture Base = 64 mills/kWh *90% CO2 Capture *Compression to 2,200 Psia *50 Mile Pipeline + Saline Formation Storage + 100 Years Monitoring 0 10 20 30 40 50 60 70 80 90 PercentIncreaseinCOE Trans., Stor., & Monit. Compression Capital Capture Capital Capture Operating Capture Steam Capture Aux. Power Compression power 2% Parasitic Power h COE by 52% Operating Cost h COE by 7% Capital Cost h COE by 27%
  • 7. Centrifugal Compression SUPPORTED BY: • High volume flows • Unique characteristics of CO2 for compressor design Real gas effects High volume reduction Low speed of sound Avoiding liquid formation
  • 8. Beam-Style Compressors SUPPORTED BY: • Commonly used in petrochemical and natural gas industries • Straight through or back-to- back configurations • Intercooling between 2 sections and/or between units • High reliability – minimal bearings/seals • High pressure – up to 15,000 psi
  • 9. Internally-geared Compressors SUPPORTED BY: • Electric motor drives large bull gear that drives multiple pinion gears with centrifugal compressors on each end • Gear speeds increase with pressure • Separate inlet and outlet flanges permit intercooling at each stage • Potential reliability issues – many bearings, seals, and unshrouded impellers
  • 10. Why interest in isothermal compression? SUPPORTED BY:
  • 11. Innovations in Compressor Design SUPPORTED BY: • Internally-cooled compressor stage Performance of internally-geared compressor Reliability of beam-style compressor Reduced overall footprint ─ Red - CO2 flow path through compressor stage ─ Blue - Liquid cooling in the diaphragm ─ Grey - Solid
  • 12. Innovations in Compressor Design SUPPORTED BY: • Supersonic shock wave compression 1/10th the physical size 40 – 50% of the installed capital cost Heat integration to offset energy penalty 10:1 compression ratio 2-stage system
  • 16.
  • 17. CO2 Transport Hazards SUPPORTED BY: •Low temperature releases •High pressures •Corrosion •High vapour density •Detection issues
  • 18. CO2 Transport Hazards • CO2 can be tolerated in quite high concentrations without permanent risk to health • BUT if those exposed have key tasks to execute their response may be impaired • THUS need to consider effects during emergency situations SUPPORTED BY:
  • 20. Thank you! INTRODUCTION TO CAPTURE, USE AND GEOLOGICAL STORAGE OF CO2 January 22-23 2015 University of Sonora, Hermosillo SUPPORTED BY: