DC Field | Value | Language |
---|---|---|
dc.contributor.author | Park, Sung Youl | ko |
dc.contributor.author | Yi, Kwang Bok | ko |
dc.contributor.author | Ko, Chang Hyun | ko |
dc.contributor.author | Park, Jong-Ho | ko |
dc.contributor.author | Kim, Jong-Nam | ko |
dc.contributor.author | Hong, Won-Hi | ko |
dc.date.accessioned | 2013-03-08T20:24:29Z | - |
dc.date.available | 2013-03-08T20:24:29Z | - |
dc.date.created | 2012-02-06 | - |
dc.date.created | 2012-02-06 | - |
dc.date.issued | 2010-06 | - |
dc.identifier.citation | ENERGY & FUELS, v.24, pp.3704 - 3709 | - |
dc.identifier.issn | 0887-0624 | - |
dc.identifier.uri | http://hdl.handle.net/10203/94199 | - |
dc.description.abstract | The optimal conditions of the absorbent concentration, rich CO2 loading, and regeneration temperature in a continuous CO2-capture process using a 3-27 wt % aqueous NH3 solution were experimentally studied and compared to vapor-liquid equilibrium of a CO2-NH3-H2O system. The dependence of CO, removal efficiency upon the NH3 concentration and regeneration temperature was well-explained by the regeneration critical condition, which was defined using mole fractions of CO2, NH3, and H2O in the vapor phase at equilibrium. The optimal conditions were 12 wt % NH3 concentration, 0.36 rich CO2 loading, and a 90 degrees C regeneration temperature. Use of the vapor-liquid equilibrium data of the CO2-NH3-H2O system at regeneration conditions can be employed as a method to select the optimal operating conditions of a regeneration system and can provide guidelines for the design and operation of CO2-capture process using aqueous NH3 solution. | - |
dc.language | English | - |
dc.publisher | AMER CHEMICAL SOC | - |
dc.subject | CO2 GREENHOUSE-GAS | - |
dc.subject | CARBON-DIOXIDE | - |
dc.subject | ABSORPTION | - |
dc.subject | CAPTURE | - |
dc.subject | KINETICS | - |
dc.subject | ENERGY | - |
dc.subject | 2-AMINO-2-METHYL-1-PROPANOL | - |
dc.subject | MONOETHANOLAMINE | - |
dc.subject | SEQUESTRATION | - |
dc.subject | EQUILIBRIA | - |
dc.title | Selection of Optimal Operating Conditions for a Continuous CO2-Capture Process Using an Aqueous Ammonia Solution | - |
dc.type | Article | - |
dc.identifier.wosid | 000278851200058 | - |
dc.identifier.scopusid | 2-s2.0-77953784514 | - |
dc.type.rims | ART | - |
dc.citation.volume | 24 | - |
dc.citation.beginningpage | 3704 | - |
dc.citation.endingpage | 3709 | - |
dc.citation.publicationname | ENERGY & FUELS | - |
dc.identifier.doi | 10.1021/ef100292t | - |
dc.contributor.localauthor | Hong, Won-Hi | - |
dc.contributor.nonIdAuthor | Yi, Kwang Bok | - |
dc.contributor.nonIdAuthor | Ko, Chang Hyun | - |
dc.contributor.nonIdAuthor | Park, Jong-Ho | - |
dc.contributor.nonIdAuthor | Kim, Jong-Nam | - |
dc.type.journalArticle | Article | - |
dc.subject.keywordPlus | CO2 GREENHOUSE-GAS | - |
dc.subject.keywordPlus | CARBON-DIOXIDE | - |
dc.subject.keywordPlus | ABSORPTION | - |
dc.subject.keywordPlus | CAPTURE | - |
dc.subject.keywordPlus | KINETICS | - |
dc.subject.keywordPlus | ENERGY | - |
dc.subject.keywordPlus | 2-AMINO-2-METHYL-1-PROPANOL | - |
dc.subject.keywordPlus | MONOETHANOLAMINE | - |
dc.subject.keywordPlus | SEQUESTRATION | - |
dc.subject.keywordPlus | EQUILIBRIA | - |
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