2009
DOI: 10.1016/j.cryogenics.2008.08.006
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Thermodynamic design of methane liquefaction system based on reversed-Brayton cycle

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Cited by 58 publications
(26 citation statements)
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“…1. Since the saturation (sublimation) pressure of CO 2 at LNG temperature (112 K) is 0.57 Pa, the mole fraction of CO 2 can be made less than 6 ppm at the point where CH 4 begins to condense, if the mixture is at atmospheric or higher pressure. For a long term operation, two identical heat exchangers are installed in parallel so that they can alternately capture or release CO 2 by periodically switching the flow directions.…”
Section: Introductionmentioning
confidence: 99%
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“…1. Since the saturation (sublimation) pressure of CO 2 at LNG temperature (112 K) is 0.57 Pa, the mole fraction of CO 2 can be made less than 6 ppm at the point where CH 4 begins to condense, if the mixture is at atmospheric or higher pressure. For a long term operation, two identical heat exchangers are installed in parallel so that they can alternately capture or release CO 2 by periodically switching the flow directions.…”
Section: Introductionmentioning
confidence: 99%
“…A number of standard gas separation methods are applicable to the removal of CO 2 , including membrane, physical or chemical scrubbing, temperature or pressure swing adsorption (TSA or PSA), and distillation. The pilot-scale systems under recent development in U.S.A. (1,2) , China (3) , and Korea (4) have an LNG production rate at 160~2,350…”
Section: Introductionmentioning
confidence: 99%
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