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Carbon Sequestration
CO2 Capture

CO2 Capture
Project Descriptions
PC Plant

CO2 capture is the separation of CO2 from emissions sources or the atmosphere and the recovery of a concentrated stream of CO2 that is amenable to sequestration or conversion. The program currently funds a relatively large number of laboratory-to-pilot-scale research projects involving chemical sorbents, physical sorbents, membranes, hydrates, and other approaches.  Efforts are focused on systems for capturing CO2 from coal-fired power plants, although the technologies developed will be applicable to natural-gas -fired power plants, industrial CO2 sources, and other applications. 

Pulverized coal (PC) plants, which are 99 percent of all coal-fired power plants in the United States, burn coal in air to raise steam. 
CO2 is exhausted in the flue gas at atmospheric pressure and a concentration of 10-15 volume percent.  This post-combustion
capture of CO2 is a challenging application because:

  • The low pressure and dilute concentration dictate a high actual volume of gas to be treated
  • Trace impurities in the flue gas tend to reduce the effectiveness of the CO2 adsorbing processes
  • Compressing captured CO2 from atmospheric pressure to pipeline pressure (1,200–2,000 pounds per square inch (psi)) represents a large parasitic load.

Aqueous amines are the state-of-the-art technology for CO2 capture for PC power plants.  Analysis conducted at NETL shows that CO2 capture and compression using amines raises the cost of electricity from a newly-built supercritical PC power plant by 84 percent, from 4.9 cents/kWh to 9.0 cents/kWh.  The goal for advanced CO2 capture systems is that CO2 capture and compression added to a newly constructed power plant increases the cost of electricity by no more than 20 percent compared to a no-capture case. 

Integrated gasification combined cycle (IGCC) is an exciting and emerging technology for coal power, offering the potential for higher efficiency and reduced cost of pollutant emissions control.  From the perspective of carbon sequestration, CO2 can be captured from a synthesis gas (coming out of the coal gasification reactor) before it is mixed with air in a combustion turbine. This is referred to as pre-combustion CO2 capture. The CO2 is relatively concentrated (50 volume %) and at high pressure.  These conditions offer the opportunity for lower cost CO2 capture. 

The state-of-the-art for CO2 capture from an IGCC power plant is glycol-based Selexol sorbent.  Analysis conducted at NETL shows that CO2 capture and compression using Selexol raises the cost of electricity from a newly built IGCC power plant by 25 percent, from 5.5 cents/kWh to 6.5 cents/kWh.  The goal for advanced CO2 capture and sequestration systems applied to an IGCC is no more than a 10 percent increase in the cost of electricity.  It is a more stringent goal given that the conditions for CO2 capture are more favorable in an IGCC plant.

Oxygen Combustion (oxy-combustion) combusts coal in an enriched oxygen environment using pure oxygen diluted with recycled CO2 or H2 O. The CO2 is then captured by condensing the water in the exhaust stream. Oxy-combustion offers several benefits as determined through large-scale laboratory testing and systems analysis. Oxy-combustion results in a 60-70 percent reduction in NOx emissions and increased mercury removal. Also, oxy-combustion’s key process principles have been demonstrated commercially, including air separation and flue gas recycle. The oxygen required for oxy-combustion increases costs, but novel oxygen separation techniques such as ion transport membranes and chemical looping systems are being developed to reduce costs.

Did you know? Roughly one third of U.S. carbon emissions come from power plants. Flue gas from the 300 GW of U.S. PC boiler capacity contains 12-18% CO2 by volume, exhausted at 10-15 psi. Flue gas from natural gas combined cylce plants contains from 3-6% CO2. Currently amine scrubbing with CO2 compression to 2,200 psi costs roughly 2,900 $/kW and reduces the net power plant output by 30%. Ten oxygen-fired gasifiers can provide a stream of primarily Hydrogen and CO2 at 400-800 psi. Regenerable glycol solvents can capture CO2 from these systems to produce pure CO2 at 50-300 psi.