摘要
Desublimation-based cryogenic carbon capture has drawn particular attention to mitigate the climate issue of global warming. Turbo-expander based refrigeration system is a potential option to provide cooling at 150 K for CO2 desublimation, while the CO2 spontaneous desublimation in turbo-expander complicates the expansion process and leads to wetness losses. In this paper, the non-equilibrium desublimation process is included in the one-dimensional mean streamline model of a cryogenic turbo-expander, and the expansion process with CO2 desublimation in air is investigated. The distribution of CO2 desublimation parameters in the flow passage of turbo-expander is obtained, and the two-phase expansion processes are classified into two types including desublimation expansion and subcooled expansion. A parametric study shows that a decrease in inlet temperature, an increase in pressure ratio and inlet CO2 concentration lead to a larger wetness loss, where inlet temperature is the most important parameter, followed by pressure ratio and inlet CO2 concentration. For a turbo-expander with inlet pressure of 300 kPa and CO2 concentration of 0.64%, the significant desublimation occurs at a subcooling degree of 23.7 K, leading to a wetness loss of 1.2%. To avoid desublimation as well as wetness loss in passage of a turbo-expander, the designed maximum subcooling degree is supposed to be smaller than 15 K for the turbo-expander of a cryogenic carbon capture system.
| 源语言 | 英语 |
|---|---|
| 文章编号 | 106528 |
| 期刊 | International Communications in Heat and Mass Transfer |
| 卷 | 140 |
| DOI | |
| 出版状态 | 已出版 - 1月 2023 |
联合国可持续发展目标
此成果有助于实现下列可持续发展目标:
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可持续发展目标 13 气候行动
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