Carbon Dioxide Liquefaction Process for Ship Transportation. Lee, U., Yang, S., Jeong, Y., Jung, J., Lim, Y., & Han, C. Volume 30 , 2012. doi abstract bibtex In this study, an optimal carbon dioxide liquefaction process is studied. This process uses multistage expansion and the cold vapor streams are directly mixed with compressor input streams in order to enhance the compressor efficiency. Consequently, this process does not employ expensive additional multi stage heat exchanger and operates system more efficiently. The optimal operation condition is also achieved by compressor ratio optimization using constrained nonlinear programming. As a result, about 99.1 KWh/ton C02 is consumed which is only 92.8% of total operation energy of existing carbon dioxide liquefaction process. © 2012 Elsevier B.V.
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abstract = {In this study, an optimal carbon dioxide liquefaction process is studied. This process uses multistage expansion and the cold vapor streams are directly mixed with compressor input streams in order to enhance the compressor efficiency. Consequently, this process does not employ expensive additional multi stage heat exchanger and operates system more efficiently. The optimal operation condition is also achieved by compressor ratio optimization using constrained nonlinear programming. As a result, about 99.1 KWh/ton C02 is consumed which is only 92.8% of total operation energy of existing carbon dioxide liquefaction process. © 2012 Elsevier B.V.},
bibtype = {book},
author = {Lee, U. and Yang, S. and Jeong, Y.S. and Jung, J. and Lim, Y. and Han, C.},
doi = {10.1016/B978-0-444-59519-5.50049-6}
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