Characteristics of one-dimensional bubbly flow interfacial area transport in horizontal narrow rectangular channel.
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| Title: | Characteristics of one-dimensional bubbly flow interfacial area transport in horizontal narrow rectangular channel. |
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| Authors: | Liu, Antai1 (AUTHOR), Cheng, Linhai1 (AUTHOR), Yan, Changqi1 (AUTHOR), Gu, Haifeng1 (AUTHOR) guhaifeng@hrbeu.edu.cn, Meng, Zhaoming1 (AUTHOR) |
| Source: | Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers Part A. Jan2023, Vol. 189, p30-45. 16p. |
| Subjects: | One-dimensional flow, Liquid films, Transport equation, Porosity, Film flow, Two-phase flow, Adiabatic flow, Interfacial friction |
| Abstract: | The experiments of horizontal adiabatic air-water flow in narrow rectangular channel with a cross-sectional area of 68 mm × 1.9 mm were conducted under an atmosphere pressure condition in order to study bubbly flow interfacial area transport phenomenon. The liquid film thickness was obtained by PCB liquid film sensor. The results show that the liquid film thickness can be correlated with the product of Capillary number Ca and j g / j l , so a correlation for liquid film thickness was proposed. The effect of liquid film thickness on IAC and void fraction was also evaluated. The results show that the average error caused by ignoring liquid film thickness is about 6.1% and 10.1%, respectively. The lateral profiles and axial direction development of the void fraction, interfacial area concentration, bubble Sauter mean diameter were obtained by high-speed camera at three axial locations of Z/D = 63, 241 and 510. The simplified one-dimensional, steady-state, one-group interfacial area transport equation for an adiabatic bubbly flow with six sets of IAC source and sink models was evaluated by the current experimental data. The evaluation results showed that the models of Yao and Morel (2004) and Shen and Hibiki (2013) performed better with mean prediction errors of 12.13% and 18.92%, respectively. • Experiments of two-phase flow were conducted in a horizontal narrow rectangular. • The bubbly flow liquid film thickness was measured by PCB sensor. • The lateral and axial development of the interfacial parameters were obtained. • The source models and sink models of Yao and Morel (2004) performed better. [ABSTRACT FROM AUTHOR] |
| Copyright of Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers Part A is the property of Elsevier B.V. and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract. (Copyright applies to all Abstracts.) | |
| Database: | Engineering Source |
| FullText | Text: Availability: 0 |
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| Header | DbId: egs DbLabel: Engineering Source An: 160963508 AccessLevel: 6 PubType: Academic Journal PubTypeId: academicJournal PreciseRelevancyScore: 0 |
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| Items | – Name: Title Label: Title Group: Ti Data: Characteristics of one-dimensional bubbly flow interfacial area transport in horizontal narrow rectangular channel. – Name: Author Label: Authors Group: Au Data: <searchLink fieldCode="AR" term="%22Liu%2C+Antai%22">Liu, Antai</searchLink><relatesTo>1</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Cheng%2C+Linhai%22">Cheng, Linhai</searchLink><relatesTo>1</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Yan%2C+Changqi%22">Yan, Changqi</searchLink><relatesTo>1</relatesTo> (AUTHOR)<br /><searchLink fieldCode="AR" term="%22Gu%2C+Haifeng%22">Gu, Haifeng</searchLink><relatesTo>1</relatesTo> (AUTHOR)<i> guhaifeng@hrbeu.edu.cn</i><br /><searchLink fieldCode="AR" term="%22Meng%2C+Zhaoming%22">Meng, Zhaoming</searchLink><relatesTo>1</relatesTo> (AUTHOR) – Name: TitleSource Label: Source Group: Src Data: <searchLink fieldCode="JN" term="%22Chemical+Engineering+Research+%26+Design%3A+Transactions+of+the+Institution+of+Chemical+Engineers+Part+A%22">Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers Part A</searchLink>. Jan2023, Vol. 189, p30-45. 16p. – Name: Subject Label: Subjects Group: Su Data: <searchLink fieldCode="DE" term="%22One-dimensional+flow%22">One-dimensional flow</searchLink><br /><searchLink fieldCode="DE" term="%22Liquid+films%22">Liquid films</searchLink><br /><searchLink fieldCode="DE" term="%22Transport+equation%22">Transport equation</searchLink><br /><searchLink fieldCode="DE" term="%22Porosity%22">Porosity</searchLink><br /><searchLink fieldCode="DE" term="%22Film+flow%22">Film flow</searchLink><br /><searchLink fieldCode="DE" term="%22Two-phase+flow%22">Two-phase flow</searchLink><br /><searchLink fieldCode="DE" term="%22Adiabatic+flow%22">Adiabatic flow</searchLink><br /><searchLink fieldCode="DE" term="%22Interfacial+friction%22">Interfacial friction</searchLink> – Name: Abstract Label: Abstract Group: Ab Data: The experiments of horizontal adiabatic air-water flow in narrow rectangular channel with a cross-sectional area of 68 mm × 1.9 mm were conducted under an atmosphere pressure condition in order to study bubbly flow interfacial area transport phenomenon. The liquid film thickness was obtained by PCB liquid film sensor. The results show that the liquid film thickness can be correlated with the product of Capillary number Ca and j g / j l , so a correlation for liquid film thickness was proposed. The effect of liquid film thickness on IAC and void fraction was also evaluated. The results show that the average error caused by ignoring liquid film thickness is about 6.1% and 10.1%, respectively. The lateral profiles and axial direction development of the void fraction, interfacial area concentration, bubble Sauter mean diameter were obtained by high-speed camera at three axial locations of Z/D = 63, 241 and 510. The simplified one-dimensional, steady-state, one-group interfacial area transport equation for an adiabatic bubbly flow with six sets of IAC source and sink models was evaluated by the current experimental data. The evaluation results showed that the models of Yao and Morel (2004) and Shen and Hibiki (2013) performed better with mean prediction errors of 12.13% and 18.92%, respectively. • Experiments of two-phase flow were conducted in a horizontal narrow rectangular. • The bubbly flow liquid film thickness was measured by PCB sensor. • The lateral and axial development of the interfacial parameters were obtained. • The source models and sink models of Yao and Morel (2004) performed better. [ABSTRACT FROM AUTHOR] – Name: AbstractSuppliedCopyright Label: Group: Ab Data: <i>Copyright of Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers Part A is the property of Elsevier B.V. and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract.</i> (Copyright applies to all Abstracts.) |
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| RecordInfo | BibRecord: BibEntity: Identifiers: – Type: doi Value: 10.1016/j.cherd.2022.10.039 Languages: – Code: eng Text: English PhysicalDescription: Pagination: PageCount: 16 StartPage: 30 Subjects: – SubjectFull: One-dimensional flow Type: general – SubjectFull: Liquid films Type: general – SubjectFull: Transport equation Type: general – SubjectFull: Porosity Type: general – SubjectFull: Film flow Type: general – SubjectFull: Two-phase flow Type: general – SubjectFull: Adiabatic flow Type: general – SubjectFull: Interfacial friction Type: general Titles: – TitleFull: Characteristics of one-dimensional bubbly flow interfacial area transport in horizontal narrow rectangular channel. Type: main BibRelationships: HasContributorRelationships: – PersonEntity: Name: NameFull: Liu, Antai – PersonEntity: Name: NameFull: Cheng, Linhai – PersonEntity: Name: NameFull: Yan, Changqi – PersonEntity: Name: NameFull: Gu, Haifeng – PersonEntity: Name: NameFull: Meng, Zhaoming IsPartOfRelationships: – BibEntity: Dates: – D: 01 M: 01 Text: Jan2023 Type: published Y: 2023 Identifiers: – Type: issn-print Value: 02638762 Numbering: – Type: volume Value: 189 Titles: – TitleFull: Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers Part A Type: main |
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