Experimental Investigation of Heat Transfer in Two-phase Flow Boiling
In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass flu...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
T-W Lim [verfasserIn] |
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| Format: |
Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2015 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Experimental heat transfer - Washington, DC : Taylor & Francis, 1987, 28(2015), 1, Seite 23-36 |
|---|---|
| Übergeordnetes Werk: |
volume:28 ; year:2015 ; number:1 ; pages:23-36 |
| Links: |
|---|
| DOI / URN: |
10.1080/08916152.2013.803173 |
|---|
| Katalog-ID: |
OLC1958012068 |
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| 520 | |a In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. | ||
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10.1080/08916152.2013.803173 doi PQ20160617 (DE-627)OLC1958012068 (DE-599)GBVOLC1958012068 (PRQ)c2868-7cae0d84e0bf8a5b97f7308d086f1edebec657984ff0a23890ac749a3917425f0 (KEY)0167565620150000028000100023experimentalinvestigationofheattransferintwophasef DE-627 ger DE-627 rakwb eng 600 DNB 50.38 bkl 50.33 bkl T-W Lim verfasserin aut Experimental Investigation of Heat Transfer in Two-phase Flow Boiling 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. Water flow Reynolds number Heat transfer S-S You oth J-H Choi oth H-S Kim oth Enthalten in Experimental heat transfer Washington, DC : Taylor & Francis, 1987 28(2015), 1, Seite 23-36 (DE-627)12925052X (DE-600)59563-9 (DE-576)018613640 0891-6152 nnns volume:28 year:2015 number:1 pages:23-36 http://dx.doi.org/10.1080/08916152.2013.803173 Volltext http://search.proquest.com/docview/1553746216 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_70 GBV_ILN_2016 GBV_ILN_2118 50.38 AVZ 50.33 AVZ AR 28 2015 1 23-36 |
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10.1080/08916152.2013.803173 doi PQ20160617 (DE-627)OLC1958012068 (DE-599)GBVOLC1958012068 (PRQ)c2868-7cae0d84e0bf8a5b97f7308d086f1edebec657984ff0a23890ac749a3917425f0 (KEY)0167565620150000028000100023experimentalinvestigationofheattransferintwophasef DE-627 ger DE-627 rakwb eng 600 DNB 50.38 bkl 50.33 bkl T-W Lim verfasserin aut Experimental Investigation of Heat Transfer in Two-phase Flow Boiling 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. Water flow Reynolds number Heat transfer S-S You oth J-H Choi oth H-S Kim oth Enthalten in Experimental heat transfer Washington, DC : Taylor & Francis, 1987 28(2015), 1, Seite 23-36 (DE-627)12925052X (DE-600)59563-9 (DE-576)018613640 0891-6152 nnns volume:28 year:2015 number:1 pages:23-36 http://dx.doi.org/10.1080/08916152.2013.803173 Volltext http://search.proquest.com/docview/1553746216 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_70 GBV_ILN_2016 GBV_ILN_2118 50.38 AVZ 50.33 AVZ AR 28 2015 1 23-36 |
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10.1080/08916152.2013.803173 doi PQ20160617 (DE-627)OLC1958012068 (DE-599)GBVOLC1958012068 (PRQ)c2868-7cae0d84e0bf8a5b97f7308d086f1edebec657984ff0a23890ac749a3917425f0 (KEY)0167565620150000028000100023experimentalinvestigationofheattransferintwophasef DE-627 ger DE-627 rakwb eng 600 DNB 50.38 bkl 50.33 bkl T-W Lim verfasserin aut Experimental Investigation of Heat Transfer in Two-phase Flow Boiling 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. Water flow Reynolds number Heat transfer S-S You oth J-H Choi oth H-S Kim oth Enthalten in Experimental heat transfer Washington, DC : Taylor & Francis, 1987 28(2015), 1, Seite 23-36 (DE-627)12925052X (DE-600)59563-9 (DE-576)018613640 0891-6152 nnns volume:28 year:2015 number:1 pages:23-36 http://dx.doi.org/10.1080/08916152.2013.803173 Volltext http://search.proquest.com/docview/1553746216 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_70 GBV_ILN_2016 GBV_ILN_2118 50.38 AVZ 50.33 AVZ AR 28 2015 1 23-36 |
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10.1080/08916152.2013.803173 doi PQ20160617 (DE-627)OLC1958012068 (DE-599)GBVOLC1958012068 (PRQ)c2868-7cae0d84e0bf8a5b97f7308d086f1edebec657984ff0a23890ac749a3917425f0 (KEY)0167565620150000028000100023experimentalinvestigationofheattransferintwophasef DE-627 ger DE-627 rakwb eng 600 DNB 50.38 bkl 50.33 bkl T-W Lim verfasserin aut Experimental Investigation of Heat Transfer in Two-phase Flow Boiling 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. Water flow Reynolds number Heat transfer S-S You oth J-H Choi oth H-S Kim oth Enthalten in Experimental heat transfer Washington, DC : Taylor & Francis, 1987 28(2015), 1, Seite 23-36 (DE-627)12925052X (DE-600)59563-9 (DE-576)018613640 0891-6152 nnns volume:28 year:2015 number:1 pages:23-36 http://dx.doi.org/10.1080/08916152.2013.803173 Volltext http://search.proquest.com/docview/1553746216 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_70 GBV_ILN_2016 GBV_ILN_2118 50.38 AVZ 50.33 AVZ AR 28 2015 1 23-36 |
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10.1080/08916152.2013.803173 doi PQ20160617 (DE-627)OLC1958012068 (DE-599)GBVOLC1958012068 (PRQ)c2868-7cae0d84e0bf8a5b97f7308d086f1edebec657984ff0a23890ac749a3917425f0 (KEY)0167565620150000028000100023experimentalinvestigationofheattransferintwophasef DE-627 ger DE-627 rakwb eng 600 DNB 50.38 bkl 50.33 bkl T-W Lim verfasserin aut Experimental Investigation of Heat Transfer in Two-phase Flow Boiling 2015 Text txt rdacontent ohne Hilfsmittel zu benutzen n rdamedia Band nc rdacarrier In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. Water flow Reynolds number Heat transfer S-S You oth J-H Choi oth H-S Kim oth Enthalten in Experimental heat transfer Washington, DC : Taylor & Francis, 1987 28(2015), 1, Seite 23-36 (DE-627)12925052X (DE-600)59563-9 (DE-576)018613640 0891-6152 nnns volume:28 year:2015 number:1 pages:23-36 http://dx.doi.org/10.1080/08916152.2013.803173 Volltext http://search.proquest.com/docview/1553746216 GBV_USEFLAG_A SYSFLAG_A GBV_OLC SSG-OLC-TEC SSG-OLC-PHY GBV_ILN_70 GBV_ILN_2016 GBV_ILN_2118 50.38 AVZ 50.33 AVZ AR 28 2015 1 23-36 |
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Experimental Investigation of Heat Transfer in Two-phase Flow Boiling |
| abstract |
In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. |
| abstractGer |
In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. |
| abstract_unstemmed |
In this article, an experimental investigation is performed to measure the boiling heat transfer coefficient of water flow in a microchannel with a hydraulic diameter of 500 μm. Experimental tests are conducted with heat fluxes ranging from 100 to 400 kW/m2, vapor quality from 0 to 0.2, and mass fluxes of 200, 400, and 600 kg/m2s. Also, this study has modified the liquid Froude number to present a flow pattern transition toward an annular flow. Experimental results show that the flow boiling heat transfer coefficient is not dependent on mass flux and vapor quality but on heat flux to a certain degree. The measured heat transfer coefficient is compared with a few available correlations proposed for macroscales, and it is found that previous correlations have overestimated the flow boiling heat transfer coefficient for the test conditions considered in this work. This article proposes a new correlation model regarding the boiling heat transfer coefficient in mini- and microchannels using boiling number, Reynolds number, and modified Froude number. |
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| title_short |
Experimental Investigation of Heat Transfer in Two-phase Flow Boiling |
| url |
http://dx.doi.org/10.1080/08916152.2013.803173 http://search.proquest.com/docview/1553746216 |
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false |
| author2 |
S-S You J-H Choi H-S Kim |
| author2Str |
S-S You J-H Choi H-S Kim |
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12925052X |
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| doi_str |
10.1080/08916152.2013.803173 |
| up_date |
2024-07-04T01:56:48.638Z |
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