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Gas hydrate formation method to capture the carbon dioxide for pre-combustion process in IGCC plant

โœ Scribed by Soo Min Kim; Ju Dong Lee; Hyun Ju Lee; Eun Kyung Lee; Yangdo Kim


Book ID
103832804
Publisher
Elsevier Science
Year
2011
Tongue
English
Weight
709 KB
Volume
36
Category
Article
ISSN
0360-3199

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โœฆ Synopsis


In this study, we investigated the effect of tetra-n-butyl ammonium bromide (TBAB) on separation and/or collection of CO 2 from CO 2 /H 2 (40:60) gas mixture via hydrate crystallization. The phase equilibrium conditions shifted to milder conditions as increasing the amount of TBAB additive up to 3.0 mol%. The existence of the critical concentration of the additive effects on the phase equilibrium conditions was also observed. The hydrate formation rate in 1.0 mol% TBAB solution showed the highest value while the hydrate formation rate in 3.0 mol% TBAB solution showed the lowest value. Raman analyses revealed that only CO 2 gas molecules enclathrated under experimental conditions carried out in this study. The phase equilibrium temperature of CO 2 eH 2 (40:60) mixture gas hydrate systems with TBAB additive located in the range of between 283 and 290 K at the integrated gasification combined cycle (IGCC) process pressure range of 2.5e5.0 MPa. This study provides the potential of hydrate process to separate the CO 2 gas from CO 2 eH 2 (40:60) mixture gas in IGCC process without significantly lowering the processing temperature.


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