2007
DOI: 10.1016/j.jhazmat.2007.06.086
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The clathrate hydrate process for post and pre-combustion capture of carbon dioxide

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Cited by 469 publications
(331 citation statements)
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“…The dry molar (%) gas compositions of the binary gas mixtures were determined by gas chromatography and are as follows: CO 2 (17.0)/N 2 (83.0) for the model flue gas and CO 2 (40.0)/H 2 (60%) for the model fuel gas mixture. Since N 2 and O 2 form hydrate at approximately the same pressure/temperature conditions, the above CO 2 /N 2 mixture is considered a suitable model flue gas (Kang and Lee, 2000;Linga et al, 2007a). THF was supplied by Fisher Scientific with 99% purity.…”
Section: Methodsmentioning
confidence: 99%
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“…The dry molar (%) gas compositions of the binary gas mixtures were determined by gas chromatography and are as follows: CO 2 (17.0)/N 2 (83.0) for the model flue gas and CO 2 (40.0)/H 2 (60%) for the model fuel gas mixture. Since N 2 and O 2 form hydrate at approximately the same pressure/temperature conditions, the above CO 2 /N 2 mixture is considered a suitable model flue gas (Kang and Lee, 2000;Linga et al, 2007a). THF was supplied by Fisher Scientific with 99% purity.…”
Section: Methodsmentioning
confidence: 99%
“…In addition, the separation factor (S.F.) is determined from the following equation (Linga et al, 2007a):…”
Section: Co 2 Recovery and Efficiencymentioning
confidence: 99%
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“…7 TBAF exhibits greater pressure reduction than TBAB. 8 According to literature 9 , the time to reach hydrate equilibrium with TBAF is about onehalf of that with TBAB and one-fourth of that with THF.…”
Section: Introductionmentioning
confidence: 92%