CFD and experimental investigation of the gas–liquid flow in the distributor of a compact heat exchanger

•Two-phase flow inside the distribution device of a compact heat exchanger has been simulated via CFD.•Distribution of the gas and liquid phase is satisfyingly reproduced.•Bubble topology and flow regimes can be predicted with the VOF approach.•This paper demonstrates that direct simulation can help...

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Published inChemical engineering research & design Vol. 92; no. 11; pp. 2361 - 2370
Main Authors Saad, Selma Ben, Gentric, Caroline, Fourmigué, Jean-François, Clément, Patrice, Leclerc, Jean-Pierre
Format Journal Article
LanguageEnglish
Published Elsevier B.V 01.11.2014
Elsevier
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Online AccessGet full text
ISSN0263-8762
1744-3563
DOI10.1016/j.cherd.2014.02.002

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Abstract •Two-phase flow inside the distribution device of a compact heat exchanger has been simulated via CFD.•Distribution of the gas and liquid phase is satisfyingly reproduced.•Bubble topology and flow regimes can be predicted with the VOF approach.•This paper demonstrates that direct simulation can help design the header of compact heat exchangers. High performance of compact heat exchangers is conditioned by correct fluid distribution. This is especially true for gas–liquid heat exchangers where a uniform distribution is particularly delicate to obtain and where maldistribution entails significant performance deterioration. Several phenomena can lead to phase distribution problems: the fins may be subject to manufacturing defects or fouling, leading to shortcuts or dead zones. But the first source of maldistribution may be a poor distribution at the outlet of the entrance distributor. This distributor aims at mixing the phases and distributing them across the channels. The present study deals with the simulation and experimental investigation of the two-phase distribution and flow regimes in a distributor located at the bottom of the cold flow pilot plant of a vertical compact heat exchanger. Air and water are the working fluids, and the range of superficial velocities inside the distributor is 0.9–8.8ms−1 and 0.35–0.8ms−1, for air and water respectively. Three-dimensional Volume Of Fluid (VOF) simulations are performed and compared to experimental distributions, pressure drops, and visualizations.
AbstractList High performance of compact heat exchangers is conditioned by correct fluid distribution. This is especially true for gas-liquid heat exchangers where a uniform distribution is particularly delicate to obtain and where maldistribution entails significant performance deterioration. Several phenomena can lead to phase distribution problems: the fins may be subject to manufacturing defects or fouling, leading to shortcuts or dead zones. But the first source of maldistribution may be a poor distribution at the outlet of the entrance distributor. This distributor aims at mixing the phases and distributing them across the channels. The present study deals with the simulation and experimental investigation of the two-phase distribution and flow regimes in a distributor located at the bottom of the cold flow pilot plant of a vertical compact heat exchanger. Air and water are the working fluids, and the range of superficial velocities inside the distributor is 0.9-8.8m s(-1) and 0.35-0.8 ms(-1), for air and water respectively. Three-dimensional Volume Of Fluid (VOF) simulations are performed and compared to experimental distributions, pressure drops, and visualizations.
•Two-phase flow inside the distribution device of a compact heat exchanger has been simulated via CFD.•Distribution of the gas and liquid phase is satisfyingly reproduced.•Bubble topology and flow regimes can be predicted with the VOF approach.•This paper demonstrates that direct simulation can help design the header of compact heat exchangers. High performance of compact heat exchangers is conditioned by correct fluid distribution. This is especially true for gas–liquid heat exchangers where a uniform distribution is particularly delicate to obtain and where maldistribution entails significant performance deterioration. Several phenomena can lead to phase distribution problems: the fins may be subject to manufacturing defects or fouling, leading to shortcuts or dead zones. But the first source of maldistribution may be a poor distribution at the outlet of the entrance distributor. This distributor aims at mixing the phases and distributing them across the channels. The present study deals with the simulation and experimental investigation of the two-phase distribution and flow regimes in a distributor located at the bottom of the cold flow pilot plant of a vertical compact heat exchanger. Air and water are the working fluids, and the range of superficial velocities inside the distributor is 0.9–8.8ms−1 and 0.35–0.8ms−1, for air and water respectively. Three-dimensional Volume Of Fluid (VOF) simulations are performed and compared to experimental distributions, pressure drops, and visualizations.
High performance of compact heat exchangers is conditioned by correct fluid distribution. This is especially true for gas-liquid heat exchangers where a uniform distribution is particularly delicate to obtain and where maldistribution entails significant performance deterioration. Several phenomena can lead to phase distribution problems: the fins may be subject to manufacturing defects or fouling, leading to shortcuts or dead zones. But the first source of maldistribution may be a poor distribution at the outlet of the entrance distributor. This distributor aims at mixing the phases and distributing them across the channels. The present study deals with the simulation and experimental investigation of the two-phase distribution and flow regimes in a distributor located at the bottom of the cold flow pilot plant of a vertical compact heat exchanger. Air and water are the working fluids, and the range of superficial velocities inside the distributor is 0.9-8.8 m s super(-1) and 0.35-0.8 ms super(-1), for air and water respectively. Three-dimensional Volume Of Fluid (VOF) simulations are performed and compared to experimental distributions, pressure drops, and visualizations.
Author Fourmigué, Jean-François
Clément, Patrice
Gentric, Caroline
Saad, Selma Ben
Leclerc, Jean-Pierre
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  fullname: Leclerc, Jean-Pierre
  organization: Laboratoire Réactions et Génie des Procédés (LRGP), CNRS, UMR 7274, 1, rue Grandville BP 20451, 54001 Nancy, France
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Issue 11
Keywords CFD simulation
Volume Of Fluid
Compact heat exchanger
Gas–liquid flow
Flow regimes
Gas–liquid distribution
Language English
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Snippet •Two-phase flow inside the distribution device of a compact heat exchanger has been simulated via CFD.•Distribution of the gas and liquid phase is satisfyingly...
High performance of compact heat exchangers is conditioned by correct fluid distribution. This is especially true for gas-liquid heat exchangers where a...
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SubjectTerms CFD simulation
Channels
Chemical Sciences
Compact heat exchanger
Distributors
Flow regimes
Fluid dynamics
Fluid flow
Fluids
Gas–liquid distribution
Gas–liquid flow
Heat exchangers
Simulation
Three dimensional
Volume Of Fluid
Title CFD and experimental investigation of the gas–liquid flow in the distributor of a compact heat exchanger
URI https://dx.doi.org/10.1016/j.cherd.2014.02.002
https://www.proquest.com/docview/1660044372
https://hal.univ-lorraine.fr/hal-01274043
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