Standard

Bubble diameters variation along the gas-liquid flow in a flat channel at various inclination angles. / Gorelikova, A. E.; Randin, V. V.; Chinak, A. V.

In: Thermophysics and Aeromechanics, Vol. 27, No. 5, 09.2020, p. 767-773.

Research output: Contribution to journal › Article › peer-review

Harvard

Gorelikova, AE, Randin, VV & Chinak, AV 2020, 'Bubble diameters variation along the gas-liquid flow in a flat channel at various inclination angles', Thermophysics and Aeromechanics, vol. 27, no. 5, pp. 767-773. https://doi.org/10.1134/S086986432005011X

APA

Gorelikova, A. E., Randin, V. V., & Chinak, A. V. (2020). Bubble diameters variation along the gas-liquid flow in a flat channel at various inclination angles. Thermophysics and Aeromechanics, 27(5), 767-773. https://doi.org/10.1134/S086986432005011X

Vancouver

Gorelikova AE, Randin VV, Chinak AV. Bubble diameters variation along the gas-liquid flow in a flat channel at various inclination angles. Thermophysics and Aeromechanics. 2020 Sept;27(5):767-773. doi: 10.1134/S086986432005011X

Author

Gorelikova, A. E. ; Randin, V. V. ; Chinak, A. V. / Bubble diameters variation along the gas-liquid flow in a flat channel at various inclination angles. In: Thermophysics and Aeromechanics. 2020 ; Vol. 27, No. 5. pp. 767-773.

BibTeX

@article{07a0eeeead3843e5919bf60d9b84201b,
title = "Bubble diameters variation along the gas-liquid flow in a flat channel at various inclination angles",
abstract = "The results of an experimental study of a bubble diameters variation with a distance from the gas injection point in an upward bubbly flow in an inclined flat channel are presented. The measurements were carried out for a superficial liquid velocity of 0.51 m/s (Re = 12400) and various volumetric gas flow rate ratios. It is shown that at low values of volumetric gas flow rate ratio (β < 2 %), there is almost no bubble coalescence; therefore, the channel inclination angle and distance from the point of gas injection into the liquid flow do not affect the average diameter of gas bubbles.",
keywords = "bubble diameters, bubbles, flat channel, gas-liquid flow, histograms",
author = "Gorelikova, {A. E.} and Randin, {V. V.} and Chinak, {A. V.}",
note = "Publisher Copyright: {\textcopyright} 2020, A.E. Gorelikova, V.V. Randin, and A.V. Chinak. Copyright: Copyright 2021 Elsevier B.V., All rights reserved.",
year = "2020",
month = sep,
doi = "10.1134/S086986432005011X",
language = "English",
volume = "27",
pages = "767--773",
journal = "Thermophysics and Aeromechanics",
issn = "0869-8643",
publisher = "PLEIADES PUBLISHING INC",
number = "5",

}

RIS

TY - JOUR

T1 - Bubble diameters variation along the gas-liquid flow in a flat channel at various inclination angles

AU - Gorelikova, A. E.

AU - Randin, V. V.

AU - Chinak, A. V.

N1 - Publisher Copyright: © 2020, A.E. Gorelikova, V.V. Randin, and A.V. Chinak. Copyright: Copyright 2021 Elsevier B.V., All rights reserved.

PY - 2020/9

Y1 - 2020/9

N2 - The results of an experimental study of a bubble diameters variation with a distance from the gas injection point in an upward bubbly flow in an inclined flat channel are presented. The measurements were carried out for a superficial liquid velocity of 0.51 m/s (Re = 12400) and various volumetric gas flow rate ratios. It is shown that at low values of volumetric gas flow rate ratio (β < 2 %), there is almost no bubble coalescence; therefore, the channel inclination angle and distance from the point of gas injection into the liquid flow do not affect the average diameter of gas bubbles.

AB - The results of an experimental study of a bubble diameters variation with a distance from the gas injection point in an upward bubbly flow in an inclined flat channel are presented. The measurements were carried out for a superficial liquid velocity of 0.51 m/s (Re = 12400) and various volumetric gas flow rate ratios. It is shown that at low values of volumetric gas flow rate ratio (β < 2 %), there is almost no bubble coalescence; therefore, the channel inclination angle and distance from the point of gas injection into the liquid flow do not affect the average diameter of gas bubbles.

KW - bubble diameters

KW - bubbles

KW - flat channel

KW - gas-liquid flow

KW - histograms

UR - http://www.scopus.com/inward/record.url?scp=85101135387&partnerID=8YFLogxK

U2 - 10.1134/S086986432005011X

DO - 10.1134/S086986432005011X

M3 - Article

AN - SCOPUS:85101135387

VL - 27

SP - 767

EP - 773

JO - Thermophysics and Aeromechanics

JF - Thermophysics and Aeromechanics

SN - 0869-8643

IS - 5

ER -

ID: 27965580