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Absorption-Based Post-combustion Capture of Carbon Dioxide by Paul Feron

By Paul Feron

Absorption-Based Post-Combustion seize of Carbon Dioxide presents a complete and authoritative overview of using absorbents for post-combustion seize of carbon dioxide. As fossil fuel-based strength iteration applied sciences are inclined to stay key sooner or later, no less than within the brief- and medium-term, carbon trap and garage might be a serious greenhouse gasoline aid approach.

Post-combustion catch consists of the elimination of carbon dioxide from flue gases after gasoline combustion, that means that carbon dioxide can then be compressed and cooled to shape a thoroughly portable liquid that may be saved underground.

  • Provides researchers in academia and with an authoritative evaluation of the amine-based equipment for carbon dioxide catch from flue gases and comparable processes
  • Editors and individuals are popular specialists within the field
  • Presents the 1st ebook in this particular topic

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Extra resources for Absorption-Based Post-combustion Capture of Carbon Dioxide

Example text

18] as well as in the figure we use two arrows ƒ! ƒ to repre- kÀ1 Ki sent relatively slow, observable reactions and the double arrow ! to indicate instantaneous protonation equilibria. The enthalpy of reaction is indicated by DHi. The slow, measurable reactions are the reaction of CO2 with water to form carbonic acid Eq. 11], with hydroxide to form bicarbonate Eq. 12], and with the amine to form the carbamic acid Eq. 17]. Coupled to these slow reactions are the protonation equilibria of carbonate, Eqs.

The heat of CO2 absorption and Conventional amine scrubbing for CO2 capture 45 maximum operating temperature determine the compressor, reboiler, and stripper capital cost and lost work. 1 Capacity The capital and energy cost of the cross exchanger depend on the working capacity of the absorption liquid. There will always be an economic trade-off of the exchanger size and approach temperature. The effect of absorption capacity would be eliminated with an infinitely large exchanger, but that would result in a prohibitive capital cost.

The chapter concludes with a comprehensive tabulation of liquid absorbent properties and some perspectives on economic optimization. 1 History Acid gas treating Amine scrubbing for CO2 capture from combustion gas is based on the common absorption/stripping process for removing H2S and CO2 from natural gas and other fuel gases. Fig. 1 shows the process patented by Bottoms (1930) to sweeten natural gas. Hundreds of plants have been constructed using this process for acid gas treating of natural gas and hydrogen with aqueous monoethanolamine (MEA) or other common amines.

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