Abstract
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.
| Original language | English |
|---|---|
| Article number | 106528 |
| Journal | International Communications in Heat and Mass Transfer |
| Volume | 140 |
| DOIs | |
| State | Published - Jan 2023 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 13 Climate Action
Keywords
- Cryogenic carbon capture
- Spontaneous desublimation
- Turbo-expander
- Wetness loss
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