Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics

Abstract The present paper aims to evaluate the performance of a multi-branch gas–liquid pipe separator by means of 3D computational fluid dynamics. This type of separator is attractive for deepwater subsea hydrocarbon fields due to its compactness and reduced weight when compared against traditiona...

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Main Authors: H. Refsnes, M. Diaz, M. Stanko
Format: Article
Language:English
Published: SpringerOpen 2019-06-01
Series:Journal of Petroleum Exploration and Production Technology
Subjects:
Online Access:http://link.springer.com/article/10.1007/s13202-019-0708-8
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spelling doaj-4ce5f7a802a349f7bc4da2b94cbeb0f92020-11-25T03:38:26ZengSpringerOpenJournal of Petroleum Exploration and Production Technology2190-05582190-05662019-06-01943103311210.1007/s13202-019-0708-8Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamicsH. Refsnes0M. Diaz1M. Stanko2Department of Geoscience and Petroleum, Norwegian University of Science and TechnologyDepartment of Geoscience and Petroleum, Norwegian University of Science and TechnologyDepartment of Geoscience and Petroleum, Norwegian University of Science and TechnologyAbstract The present paper aims to evaluate the performance of a multi-branch gas–liquid pipe separator by means of 3D computational fluid dynamics. This type of separator is attractive for deepwater subsea hydrocarbon fields due to its compactness and reduced weight when compared against traditional gravity vessel separators. The focus of this paper is on studying the internal flow dynamics, the separation efficiency, and the performance with changing and transient operating conditions. Numerical simulations were performed on a numerical prototype of the separator using the inhomogeneous mixture model and assuming that both phases are continuous. Sensitivity analyses were performed on gas volume fraction, outlet pressures, and considering slug flow at the inlet with periods of 2 s and 8 s. The separation efficiency was quantified by calculating the liquid carry-over and gas blowby. For most of the operational conditions studied, separation occurred primarily in pipe branches closer to the inlet while those closer to the outlet exhibited a static liquid level. Reducing the gas outlet pressure caused the height of the liquid in the branches to be reduced. The inlet gas volume fraction did not affect significantly the separation performance, the flow distribution, nor the liquid level inside the separator. Separation efficiencies were not affected significantly with the presence of slugs; however, the liquid level in the branches oscillated significantly. The results and numerical models produced by this study could potentially be used to improve the understanding of this type of separators and improve its efficiency and system-level design.http://link.springer.com/article/10.1007/s13202-019-0708-8Gas–liquid separationSubsea processingComputational fluid dynamics
collection DOAJ
language English
format Article
sources DOAJ
author H. Refsnes
M. Diaz
M. Stanko
spellingShingle H. Refsnes
M. Diaz
M. Stanko
Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics
Journal of Petroleum Exploration and Production Technology
Gas–liquid separation
Subsea processing
Computational fluid dynamics
author_facet H. Refsnes
M. Diaz
M. Stanko
author_sort H. Refsnes
title Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics
title_short Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics
title_full Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics
title_fullStr Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics
title_full_unstemmed Performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics
title_sort performance evaluation of a multi-branch gas–liquid pipe separator using computational fluid dynamics
publisher SpringerOpen
series Journal of Petroleum Exploration and Production Technology
issn 2190-0558
2190-0566
publishDate 2019-06-01
description Abstract The present paper aims to evaluate the performance of a multi-branch gas–liquid pipe separator by means of 3D computational fluid dynamics. This type of separator is attractive for deepwater subsea hydrocarbon fields due to its compactness and reduced weight when compared against traditional gravity vessel separators. The focus of this paper is on studying the internal flow dynamics, the separation efficiency, and the performance with changing and transient operating conditions. Numerical simulations were performed on a numerical prototype of the separator using the inhomogeneous mixture model and assuming that both phases are continuous. Sensitivity analyses were performed on gas volume fraction, outlet pressures, and considering slug flow at the inlet with periods of 2 s and 8 s. The separation efficiency was quantified by calculating the liquid carry-over and gas blowby. For most of the operational conditions studied, separation occurred primarily in pipe branches closer to the inlet while those closer to the outlet exhibited a static liquid level. Reducing the gas outlet pressure caused the height of the liquid in the branches to be reduced. The inlet gas volume fraction did not affect significantly the separation performance, the flow distribution, nor the liquid level inside the separator. Separation efficiencies were not affected significantly with the presence of slugs; however, the liquid level in the branches oscillated significantly. The results and numerical models produced by this study could potentially be used to improve the understanding of this type of separators and improve its efficiency and system-level design.
topic Gas–liquid separation
Subsea processing
Computational fluid dynamics
url http://link.springer.com/article/10.1007/s13202-019-0708-8
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