Lumped heat and mass transfer coefficient for simulation of a pressure swing adsorption process
The practical implications of replacing various individual transport resistances such as gas-solid mass and heat transfer, and gas phase axial dispersions of mass and heat in a numerical model of a pressure swing adsorption (PSA) process by a single, empirical, lumped, effective mass transport coeff...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Vemula, Rama Rao [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2017 |
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| Rechteinformationen: |
Nutzungsrecht: © 2017 Taylor & Francis 2017 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Separation science and technology - Philadelphia, Pa. : Taylor & Francis, 1978, 52(2017), 1, Seite 35-41 |
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| Übergeordnetes Werk: |
volume:52 ; year:2017 ; number:1 ; pages:35-41 |
| Links: |
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| DOI / URN: |
10.1080/01496395.2016.1242629 |
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| 520 | |a The practical implications of replacing various individual transport resistances such as gas-solid mass and heat transfer, and gas phase axial dispersions of mass and heat in a numerical model of a pressure swing adsorption (PSA) process by a single, empirical, lumped, effective mass transport coefficient were evaluated. A non-isothermal, adiabatic, four-step Skarstrom-like PSA process for production of pure helium from a binary helium-nitrogen mixture using 5A zeolite adsorbent was considered. It was found that the above-described model simplification was adequate to describe key process performances such as the bed size factor and the product recovery vis-a-vis a detailed model where the effects of all individual resistances were explicitly included. | ||
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10.1080/01496395.2016.1242629 doi PQ20170301 (DE-627)OLC1987112059 (DE-599)GBVOLC1987112059 (PRQ)c1267-ed758591098af3df621d46face3884216cc43ade902d98b4d93ca36c84c360990 (KEY)0017461020170000052000100035lumpedheatandmasstransfercoefficientforsimulationo DE-627 ger DE-627 rakwb eng 540 DNB Vemula, Rama Rao verfasserin aut Lumped heat and mass transfer coefficient for simulation of a pressure swing adsorption process 2017 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The practical implications of replacing various individual transport resistances such as gas-solid mass and heat transfer, and gas phase axial dispersions of mass and heat in a numerical model of a pressure swing adsorption (PSA) process by a single, empirical, lumped, effective mass transport coefficient were evaluated. A non-isothermal, adiabatic, four-step Skarstrom-like PSA process for production of pure helium from a binary helium-nitrogen mixture using 5A zeolite adsorbent was considered. It was found that the above-described model simplification was adequate to describe key process performances such as the bed size factor and the product recovery vis-a-vis a detailed model where the effects of all individual resistances were explicitly included. Nutzungsrecht: © 2017 Taylor & Francis 2017 PSA process performance Axial mass and heat dispersion numerical simulation lumped mass and heat transfer coefficient Kothare, Mayuresh V oth Sircar, Shivaji oth Enthalten in Separation science and technology Philadelphia, Pa. : Taylor & Francis, 1978 52(2017), 1, Seite 35-41 (DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 0149-6395 nnns volume:52 year:2017 number:1 pages:35-41 http://dx.doi.org/10.1080/01496395.2016.1242629 Volltext http://www.tandfonline.com/doi/abs/10.1080/01496395.2016.1242629 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 52 2017 1 35-41 |
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10.1080/01496395.2016.1242629 doi PQ20170301 (DE-627)OLC1987112059 (DE-599)GBVOLC1987112059 (PRQ)c1267-ed758591098af3df621d46face3884216cc43ade902d98b4d93ca36c84c360990 (KEY)0017461020170000052000100035lumpedheatandmasstransfercoefficientforsimulationo DE-627 ger DE-627 rakwb eng 540 DNB Vemula, Rama Rao verfasserin aut Lumped heat and mass transfer coefficient for simulation of a pressure swing adsorption process 2017 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier The practical implications of replacing various individual transport resistances such as gas-solid mass and heat transfer, and gas phase axial dispersions of mass and heat in a numerical model of a pressure swing adsorption (PSA) process by a single, empirical, lumped, effective mass transport coefficient were evaluated. A non-isothermal, adiabatic, four-step Skarstrom-like PSA process for production of pure helium from a binary helium-nitrogen mixture using 5A zeolite adsorbent was considered. It was found that the above-described model simplification was adequate to describe key process performances such as the bed size factor and the product recovery vis-a-vis a detailed model where the effects of all individual resistances were explicitly included. Nutzungsrecht: © 2017 Taylor & Francis 2017 PSA process performance Axial mass and heat dispersion numerical simulation lumped mass and heat transfer coefficient Kothare, Mayuresh V oth Sircar, Shivaji oth Enthalten in Separation science and technology Philadelphia, Pa. : Taylor & Francis, 1978 52(2017), 1, Seite 35-41 (DE-627)12994100X (DE-600)391905-5 (DE-576)015504247 0149-6395 nnns volume:52 year:2017 number:1 pages:35-41 http://dx.doi.org/10.1080/01496395.2016.1242629 Volltext http://www.tandfonline.com/doi/abs/10.1080/01496395.2016.1242629 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-CHE SSG-OLC-PHA SSG-OLC-DE-84 GBV_ILN_70 AR 52 2017 1 35-41 |
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Lumped heat and mass transfer coefficient for simulation of a pressure swing adsorption process |
| abstract |
The practical implications of replacing various individual transport resistances such as gas-solid mass and heat transfer, and gas phase axial dispersions of mass and heat in a numerical model of a pressure swing adsorption (PSA) process by a single, empirical, lumped, effective mass transport coefficient were evaluated. A non-isothermal, adiabatic, four-step Skarstrom-like PSA process for production of pure helium from a binary helium-nitrogen mixture using 5A zeolite adsorbent was considered. It was found that the above-described model simplification was adequate to describe key process performances such as the bed size factor and the product recovery vis-a-vis a detailed model where the effects of all individual resistances were explicitly included. |
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The practical implications of replacing various individual transport resistances such as gas-solid mass and heat transfer, and gas phase axial dispersions of mass and heat in a numerical model of a pressure swing adsorption (PSA) process by a single, empirical, lumped, effective mass transport coefficient were evaluated. A non-isothermal, adiabatic, four-step Skarstrom-like PSA process for production of pure helium from a binary helium-nitrogen mixture using 5A zeolite adsorbent was considered. It was found that the above-described model simplification was adequate to describe key process performances such as the bed size factor and the product recovery vis-a-vis a detailed model where the effects of all individual resistances were explicitly included. |
| abstract_unstemmed |
The practical implications of replacing various individual transport resistances such as gas-solid mass and heat transfer, and gas phase axial dispersions of mass and heat in a numerical model of a pressure swing adsorption (PSA) process by a single, empirical, lumped, effective mass transport coefficient were evaluated. A non-isothermal, adiabatic, four-step Skarstrom-like PSA process for production of pure helium from a binary helium-nitrogen mixture using 5A zeolite adsorbent was considered. It was found that the above-described model simplification was adequate to describe key process performances such as the bed size factor and the product recovery vis-a-vis a detailed model where the effects of all individual resistances were explicitly included. |
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| title_short |
Lumped heat and mass transfer coefficient for simulation of a pressure swing adsorption process |
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http://dx.doi.org/10.1080/01496395.2016.1242629 http://www.tandfonline.com/doi/abs/10.1080/01496395.2016.1242629 |
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Kothare, Mayuresh V Sircar, Shivaji |
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10.1080/01496395.2016.1242629 |
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