2007
DOI: 10.1016/j.energy.2006.08.003
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Comparative analysis of energy requirements of CO2 removal from metallurgical fuel gases

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Cited by 41 publications
(16 citation statements)
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“…Figure 4 presents the flow sheet of the Selexol CO 2 capture process (Chiesa and Consonni 1999;Lampert and Ziebik 2007). The acidic gas H 2 S is first removed from syngas 1.…”
Section: Co 2 Capture Technologiesmentioning
confidence: 99%
“…Figure 4 presents the flow sheet of the Selexol CO 2 capture process (Chiesa and Consonni 1999;Lampert and Ziebik 2007). The acidic gas H 2 S is first removed from syngas 1.…”
Section: Co 2 Capture Technologiesmentioning
confidence: 99%
“…The CO 2 physical absorption in the hybrid system is based on a model developed by Lozza and Chiesa [31] using the Selexol [32] absorption medium. A conventional gas-steam combined cycle system with CO 2 separation from the exhaust gas (CC-Post) is also simulated for the purpose of performance comparison, in which CO 2 capture is accomplished by using a chemical absorption process (with monoethanolamine (MEA) [33] as the absorbent).…”
Section: The Simulation Methods and Main Assumptionsmentioning
confidence: 99%
“…They estimated the total costs for the CO 2 recovery unit were in the range 15.0-17.5V/ton CO 2 . Lampert and Ziebik (2007) realized CO 2 removal from metallurgical fuel gases by the physical absorption process with the Selexol solvent as the absorption liquid. Furthermore, they found that the lower heating value of the gases will increase when the CO 2 content is decreased thereby resulting in better conditions for its utilizations.…”
Section: Co 2 Emission Reduction Measuresmentioning
confidence: 99%