by Professor John M. Pfotenhauer, University of Wisconsin – Madison, pfot@engr.wisc.edu

The group at the University of Oregon, which also included scientists John Elzey and Robert Hershberger, was building on an analysis by Donnelly from 1979 that proposed using a cryogenic refrigeration system to remove odiferous pollutants from the smokestacks of a local paper mill. The group conceived applying the same idea to extract not only carbon dioxide, but a variety of other pollutants such as sulfur dioxide and mercury from the effluent of coal-burning power plants. Cooling the gas flow to the point where a given component condenses from the gas phase into either the liquid or solid phase allows that component to be extracted from the gas flow. The remaining gas flow, upon re-warming to room temperature, presents a environmentally friendly stream composed primarily of nitrogen, oxygen and argon.

Using an EXCEL-based program devised by Swanson, our team’s analysis considered an incremental cooling process, for which at each step-wise reduction in temperature, the energy extracted in order to cool, condense, or de-sublimate each component in the mixture was determined according to its thermodynamic location relative to its respective phase diagram, as well as the associated work required to extract that energy. As various fractional components such as H2O, SO2 and CO2 leave the gas phase, the composition and partial pressures of the remaining gas components are adjusted.
Such an analysis should determine, for example, if the effluent from a coal plant were cooled sufficiently to extract a significant fraction, say 90 percent, of the carbon dioxide by cooling it to 153K and causing it to de-sublimate, or freeze and fall out of the gas stream, how much of the energy production from the power plant that is also producing the exhaust would be consumed by such a cooling system? Pollutants in the effluent such as sulfur dioxide and mercury would also be extracted because they would freeze out at higher temperatures. The ideal cycle analysis determined a 9.1 percent energy penalty.

The significance of these results are well summarized by the introductory paragraph of this article: “The generation of electricity through combustion of coal is the largest component of greenhouse gas emissions in the United States, and globally coal combustion constitutes 40% of carbon dioxide (CO2) emitted to the atmosphere due to energy consumption. There are two systems for capturing carbon dioxide from coal-fired power plants that have been under consideration for some time. Oxy-fuel combustion burns coal in the presence of pure oxygen and recirculated CO2 (instead of air) in order to produce a concentrated CO2 stream that is subsequently purified and compressed. The fraction of electric power loss owing to this technology is about 26%. The monoethanolamine (MEA) process passes the exhaust gases through an absorber where the MEA absorbs the CO2. The CO2 is stripped from the MEA using steam. The CO2 is then dried and compressed and the MEA is purged of contaminants and recirculated. The energy penalty for MEA is about 28%.”
Many further challenges remain before the cryogenic method for capturing carbon from the effluent of a coal-fired power plant can be put into reality. For example, reliable methods must be developed to separate solid particulates from the gas stream as the gas mixture is cooled, and to translate those solid phases into a storable liquid. Nevertheless, the scoping calculations presented in the Physical Review E article suggest an exciting opportunity for the field of cryogenics to enable a means of producing clean energy from a not-so-clean fuel.








