Visual investigation on the interface morphology of Taylor bubble and the characteristics of two-phase flow in mini-channel
A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxid...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Lu, Qi [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2015transfer abstract |
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| Schlagwörter: |
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| Umfang: |
12 |
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| Übergeordnetes Werk: |
Enthalten in: Plasticity in responses to dimensional variations of soil space in 19 grassland plant species - Dong, Ran ELSEVIER, 2022, Amsterdam [u.a.] |
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| Übergeordnetes Werk: |
volume:134 ; year:2015 ; day:29 ; month:09 ; pages:96-107 ; extent:12 |
| Links: |
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| DOI / URN: |
10.1016/j.ces.2015.04.042 |
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ELV018839924 |
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| 520 | |a A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. | ||
| 520 | |a A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. | ||
| 650 | 7 | |a Two-phase flow |2 Elsevier | |
| 650 | 7 | |a Interface morphology |2 Elsevier | |
| 650 | 7 | |a Visual investigation |2 Elsevier | |
| 650 | 7 | |a Taylor bubble |2 Elsevier | |
| 700 | 1 | |a Chen, Deqi |4 oth | |
| 700 | 1 | |a Wang, Qinghua |4 oth | |
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10.1016/j.ces.2015.04.042 doi GBVA2015020000004.pica (DE-627)ELV018839924 (ELSEVIER)S0009-2509(15)00303-6 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Lu, Qi verfasserin aut Visual investigation on the interface morphology of Taylor bubble and the characteristics of two-phase flow in mini-channel 2015transfer abstract 12 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. Two-phase flow Elsevier Interface morphology Elsevier Visual investigation Elsevier Taylor bubble Elsevier Chen, Deqi oth Wang, Qinghua oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:134 year:2015 day:29 month:09 pages:96-107 extent:12 https://doi.org/10.1016/j.ces.2015.04.042 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 134 2015 29 0929 96-107 12 045F 660 |
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10.1016/j.ces.2015.04.042 doi GBVA2015020000004.pica (DE-627)ELV018839924 (ELSEVIER)S0009-2509(15)00303-6 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Lu, Qi verfasserin aut Visual investigation on the interface morphology of Taylor bubble and the characteristics of two-phase flow in mini-channel 2015transfer abstract 12 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. Two-phase flow Elsevier Interface morphology Elsevier Visual investigation Elsevier Taylor bubble Elsevier Chen, Deqi oth Wang, Qinghua oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:134 year:2015 day:29 month:09 pages:96-107 extent:12 https://doi.org/10.1016/j.ces.2015.04.042 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 134 2015 29 0929 96-107 12 045F 660 |
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10.1016/j.ces.2015.04.042 doi GBVA2015020000004.pica (DE-627)ELV018839924 (ELSEVIER)S0009-2509(15)00303-6 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Lu, Qi verfasserin aut Visual investigation on the interface morphology of Taylor bubble and the characteristics of two-phase flow in mini-channel 2015transfer abstract 12 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. Two-phase flow Elsevier Interface morphology Elsevier Visual investigation Elsevier Taylor bubble Elsevier Chen, Deqi oth Wang, Qinghua oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:134 year:2015 day:29 month:09 pages:96-107 extent:12 https://doi.org/10.1016/j.ces.2015.04.042 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 134 2015 29 0929 96-107 12 045F 660 |
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10.1016/j.ces.2015.04.042 doi GBVA2015020000004.pica (DE-627)ELV018839924 (ELSEVIER)S0009-2509(15)00303-6 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Lu, Qi verfasserin aut Visual investigation on the interface morphology of Taylor bubble and the characteristics of two-phase flow in mini-channel 2015transfer abstract 12 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. Two-phase flow Elsevier Interface morphology Elsevier Visual investigation Elsevier Taylor bubble Elsevier Chen, Deqi oth Wang, Qinghua oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:134 year:2015 day:29 month:09 pages:96-107 extent:12 https://doi.org/10.1016/j.ces.2015.04.042 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 134 2015 29 0929 96-107 12 045F 660 |
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10.1016/j.ces.2015.04.042 doi GBVA2015020000004.pica (DE-627)ELV018839924 (ELSEVIER)S0009-2509(15)00303-6 DE-627 ger DE-627 rakwb eng 660 660 DE-600 570 630 VZ BIODIV DE-30 fid Lu, Qi verfasserin aut Visual investigation on the interface morphology of Taylor bubble and the characteristics of two-phase flow in mini-channel 2015transfer abstract 12 nicht spezifiziert zzz rdacontent nicht spezifiziert z rdamedia nicht spezifiziert zu rdacarrier A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. Two-phase flow Elsevier Interface morphology Elsevier Visual investigation Elsevier Taylor bubble Elsevier Chen, Deqi oth Wang, Qinghua oth Enthalten in Elsevier Science Dong, Ran ELSEVIER Plasticity in responses to dimensional variations of soil space in 19 grassland plant species 2022 Amsterdam [u.a.] (DE-627)ELV008347182 volume:134 year:2015 day:29 month:09 pages:96-107 extent:12 https://doi.org/10.1016/j.ces.2015.04.042 Volltext GBV_USEFLAG_U GBV_ELV SYSFLAG_U FID-BIODIV SSG-OLC-PHA AR 134 2015 29 0929 96-107 12 045F 660 |
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Enthalten in Plasticity in responses to dimensional variations of soil space in 19 grassland plant species Amsterdam [u.a.] volume:134 year:2015 day:29 month:09 pages:96-107 extent:12 |
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visual investigation on the interface morphology of taylor bubble and the characteristics of two-phase flow in mini-channel |
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Visual investigation on the interface morphology of Taylor bubble and the characteristics of two-phase flow in mini-channel |
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A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. |
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A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. |
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A visual experimental investigation on Taylor bubble behavior of two-phase flow was carried out in vertical circular channels, with the length of 1000mm and inner diameter of 1mm, 2mm, 3mm and 6mm. Deionized water was used as the liquid-phase working fluid, and air, nitrogen, argon and carbon dioxide were adopted as the gas-phase working fluids. The interface morphology of Taylor bubble was recorded by a high speed camera, and the variations of pressure drop and liquid-phase mass flux were measured simultaneously. The effects of different working conditions on the interface morphology of Taylor bubble were discussed in detail, and the effect of surface tension on the Taylor bubble behavior was investigated based on the Eo (Eötvös) number and the Mo (Morton) number. Also, the fluctuations of pressure drop and liquid-phase mass flux were analyzed in detail based on the Taylor bubble behavior. Finally, a model for prediction of the two-phase flow pressure drop in mini-channel was proposed, and this model was validated based on the experimental result with good agreement. |
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