Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and Water
To solve the problem of water carryover in the supercritical CO<sub>2</sub> separation and mining process in the CO<sub>2</sub> plume geothermal system, a three-dimensional shell-tube hollow fiber membrane absorption separator is designed in this study. A coupled species tran...
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MDPI AG
2023-11-01
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Series: | Membranes |
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Online Access: | https://www.mdpi.com/2077-0375/13/12/892 |
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author | Zongliang Qiao Yue Pan Youfei Tang Yue Cao Fengqi Si |
author_facet | Zongliang Qiao Yue Pan Youfei Tang Yue Cao Fengqi Si |
author_sort | Zongliang Qiao |
collection | DOAJ |
description | To solve the problem of water carryover in the supercritical CO<sub>2</sub> separation and mining process in the CO<sub>2</sub> plume geothermal system, a three-dimensional shell-tube hollow fiber membrane absorption separator is designed in this study. A coupled species transport model, a porous medium model, and an absorption mathematical model are established, and the flow field and separation characteristics in the circular and flat tubes are analyzed using numerical simulation. The results show that the membrane separation efficiency increases with an increase in the flatness and membrane tube length. When the inlet velocity of the mixture is 0.1 m/s, the separation efficiency can reach 75.92%. Selecting a smaller flow Reynolds number and a more significant membrane tube flatness will reduce the water mass fraction at the outlet. When adding baffles of different shapes to the membrane tube, the mixture fluid in the membrane tube meanders forward and flows in the shape of “Z” under the blocking effect of the arcuate baffles. With an increase in the number of arcuate baffles in the membrane tube, the membrane separation efficiency of the separator increases continuously. The mixture fluid flows in the membrane tube with the built-in torsional baffles in a spiral manner, and the separation efficiency of the membrane separator increases with a torsion ratio reduction in the membrane tube. |
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id | doaj.art-2bc470fc5c9e4acd9ac31f31c81ce4bf |
institution | Directory Open Access Journal |
issn | 2077-0375 |
language | English |
last_indexed | 2024-03-08T20:32:38Z |
publishDate | 2023-11-01 |
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series | Membranes |
spelling | doaj.art-2bc470fc5c9e4acd9ac31f31c81ce4bf2023-12-22T14:24:16ZengMDPI AGMembranes2077-03752023-11-01131289210.3390/membranes13120892Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and WaterZongliang Qiao0Yue Pan1Youfei Tang2Yue Cao3Fengqi Si4Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, ChinaKey Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, ChinaKey Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, ChinaKey Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, ChinaKey Laboratory of Energy Thermal Conversion and Control of Ministry of Education, Southeast University, Nanjing 210096, ChinaTo solve the problem of water carryover in the supercritical CO<sub>2</sub> separation and mining process in the CO<sub>2</sub> plume geothermal system, a three-dimensional shell-tube hollow fiber membrane absorption separator is designed in this study. A coupled species transport model, a porous medium model, and an absorption mathematical model are established, and the flow field and separation characteristics in the circular and flat tubes are analyzed using numerical simulation. The results show that the membrane separation efficiency increases with an increase in the flatness and membrane tube length. When the inlet velocity of the mixture is 0.1 m/s, the separation efficiency can reach 75.92%. Selecting a smaller flow Reynolds number and a more significant membrane tube flatness will reduce the water mass fraction at the outlet. When adding baffles of different shapes to the membrane tube, the mixture fluid in the membrane tube meanders forward and flows in the shape of “Z” under the blocking effect of the arcuate baffles. With an increase in the number of arcuate baffles in the membrane tube, the membrane separation efficiency of the separator increases continuously. The mixture fluid flows in the membrane tube with the built-in torsional baffles in a spiral manner, and the separation efficiency of the membrane separator increases with a torsion ratio reduction in the membrane tube.https://www.mdpi.com/2077-0375/13/12/892supercritical carbon dioxidemembrane–absorption separatorhollow fiber membranenumerical simulationseparation efficiency |
spellingShingle | Zongliang Qiao Yue Pan Youfei Tang Yue Cao Fengqi Si Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and Water Membranes supercritical carbon dioxide membrane–absorption separator hollow fiber membrane numerical simulation separation efficiency |
title | Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and Water |
title_full | Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and Water |
title_fullStr | Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and Water |
title_full_unstemmed | Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and Water |
title_short | Numerical Simulation of Membrane Separation Characteristics of Supercritical Carbon Dioxide and Water |
title_sort | numerical simulation of membrane separation characteristics of supercritical carbon dioxide and water |
topic | supercritical carbon dioxide membrane–absorption separator hollow fiber membrane numerical simulation separation efficiency |
url | https://www.mdpi.com/2077-0375/13/12/892 |
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