Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity Separator

The flow structure in a three-phase gas-oil-water separator and its performance was the main objective of the presented investigations, for which the Euler-Euler multiphase model to simulate the flow was used. The main assumption of the model is that secondary phases, consisting of oil and water dro...

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Main Authors: Z. Krzemianowski, M. Lackowski, T. Ochrymiuk, P. Flaszyński
Format: Article
Language:English
Published: Isfahan University of Technology 2020-01-01
Series:Journal of Applied Fluid Mechanics
Subjects:
Online Access:http://jafmonline.net/JournalArchive/download?file_ID=51726&issue_ID=1006
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spelling doaj-3e4170b25521423d8acab1cf11e170752020-11-25T00:41:49ZengIsfahan University of Technology Journal of Applied Fluid Mechanics1735-35722020-01-01133805813.Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity SeparatorZ. Krzemianowski0M. Lackowski1T. Ochrymiuk2P. Flaszyński3Institute of Fluid-Flow Machinery Polish Academy of Sciences, Fiszera 14, Gdańsk, 80-231, PolandInstitute of Fluid-Flow Machinery Polish Academy of Sciences, Fiszera 14, Gdańsk, 80-231, PolandInstitute of Fluid-Flow Machinery Polish Academy of Sciences, Fiszera 14, Gdańsk, 80-231, PolandInstitute of Fluid-Flow Machinery Polish Academy of Sciences, Fiszera 14, Gdańsk, 80-231, PolandThe flow structure in a three-phase gas-oil-water separator and its performance was the main objective of the presented investigations, for which the Euler-Euler multiphase model to simulate the flow was used. The main assumption of the model is that secondary phases, consisting of oil and water droplets, are mono-dispersed with no coalescence and breakup. The considered separator is a part of the installation operated by a drilling company. In general, the investigation of separation process is very computationally expensive and time-consuming, therefore it is desirable to search for some simplifications in order to be able to carry out engineering analysis of the processes taking place in a separator. Hence, the three-dimensional coalescer was investigated as a porous element in order to find pressure losses dependence on flow velocity, which was required to simulate the existence of coalescers and baffles. As the next step, a transient Eulerian multiphase simulations were carried out for gas-oil-water mixture in a real horizontal gravity separator for two- and three-dimensional case. Required data for calculations was derived from real exploration well. In the two-dimensional case, the worked out dependence of the pressure drop with respect to velocity was used to model the flow through the porous coalescers. In three-dimensional case, the coalescers and baffles were modelled without any simplifications. It was found that general trends can be predicted despite the simplification of the geometrical model in which coalescer and baffle geometries have been replaced by a porous medium. The calculations confirmed that the complexity of geometry requiring time-consuming calculations can be usually replaced by introducing simplifications allowing for engineering analysis of separator operation that is acceptable by the industry, because the basic parameters regarding the separation process can be determined.http://jafmonline.net/JournalArchive/download?file_ID=51726&issue_ID=1006oil separators; multiphase calculations; coalescers.
collection DOAJ
language English
format Article
sources DOAJ
author Z. Krzemianowski
M. Lackowski
T. Ochrymiuk
P. Flaszyński
spellingShingle Z. Krzemianowski
M. Lackowski
T. Ochrymiuk
P. Flaszyński
Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity Separator
Journal of Applied Fluid Mechanics
oil separators; multiphase calculations; coalescers.
author_facet Z. Krzemianowski
M. Lackowski
T. Ochrymiuk
P. Flaszyński
author_sort Z. Krzemianowski
title Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity Separator
title_short Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity Separator
title_full Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity Separator
title_fullStr Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity Separator
title_full_unstemmed Substitute model and CFD Investigations of a Coalescer in a Three-Phase Crude Oil Gravity Separator
title_sort substitute model and cfd investigations of a coalescer in a three-phase crude oil gravity separator
publisher Isfahan University of Technology
series Journal of Applied Fluid Mechanics
issn 1735-3572
publishDate 2020-01-01
description The flow structure in a three-phase gas-oil-water separator and its performance was the main objective of the presented investigations, for which the Euler-Euler multiphase model to simulate the flow was used. The main assumption of the model is that secondary phases, consisting of oil and water droplets, are mono-dispersed with no coalescence and breakup. The considered separator is a part of the installation operated by a drilling company. In general, the investigation of separation process is very computationally expensive and time-consuming, therefore it is desirable to search for some simplifications in order to be able to carry out engineering analysis of the processes taking place in a separator. Hence, the three-dimensional coalescer was investigated as a porous element in order to find pressure losses dependence on flow velocity, which was required to simulate the existence of coalescers and baffles. As the next step, a transient Eulerian multiphase simulations were carried out for gas-oil-water mixture in a real horizontal gravity separator for two- and three-dimensional case. Required data for calculations was derived from real exploration well. In the two-dimensional case, the worked out dependence of the pressure drop with respect to velocity was used to model the flow through the porous coalescers. In three-dimensional case, the coalescers and baffles were modelled without any simplifications. It was found that general trends can be predicted despite the simplification of the geometrical model in which coalescer and baffle geometries have been replaced by a porous medium. The calculations confirmed that the complexity of geometry requiring time-consuming calculations can be usually replaced by introducing simplifications allowing for engineering analysis of separator operation that is acceptable by the industry, because the basic parameters regarding the separation process can be determined.
topic oil separators; multiphase calculations; coalescers.
url http://jafmonline.net/JournalArchive/download?file_ID=51726&issue_ID=1006
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