NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE

Oil and gas offshore production headers frequently experience random trips which is suspected to be due to liquid carryover issues as a result of sudden slug generation in the production headers. These slug generations are caused by sudden increase in gas velocity which provides sufficient drag t...

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Main Author: SAM, BAN
Format: Thesis
Language:English
Published: 2017
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Online Access:http://utpedia.utp.edu.my/22082/1/BanSam_MSc_e-Thesis.pdf
http://utpedia.utp.edu.my/22082/
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spelling my-utp-utpedia.220822021-10-12T20:36:12Z http://utpedia.utp.edu.my/22082/ NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE SAM, BAN TJ Mechanical engineering and machinery Oil and gas offshore production headers frequently experience random trips which is suspected to be due to liquid carryover issues as a result of sudden slug generation in the production headers. These slug generations are caused by sudden increase in gas velocity which provides sufficient drag to allow the free surface wave to grow on gasliquid interface to a height sufficient to bridge the pipe. This hydrodynamic slugging is difficult to predict since it can occur over a wide range of gas-liquid flow conditions. Compounding the complexity is the issue of no standard consensus of applicability of numerous operational correlations associated with slugging, e.g. pressure gradient, liquid holdup and slugging frequency. The objective of this study is to investigate oilgas slug formation in horizontal straight pipe and its associated pressure gradient, slug liquid holdup and slug frequency. The abrupt change in gas/liquid velocities, which causes transition of flow patterns was analyzed by using FLUENT 16.1. The incompressible Volume of Fluid (VOF) method was used to capture the transient distribution of segregated gas-liquid interface in different flow patterns. The validity of present model and its methodology was compared using Baker chart for 3.15 inches diameter horizontal pipe. The numerical solution was also compared quantitatively with existing experimental data to ensure its correctness. Finally, analyses were carried out for oil and gas vapor flow, covering substantial region of slug flow regime map. Concurrently, slug pressure gradient, liquid holdup and frequency were extracted numerically, and compared to existing empirical correlations. The present results compares favorably with some correlations and identified some outlier empirical models, which may not be suitable for operational usage. 2017-07 Thesis NonPeerReviewed application/pdf en http://utpedia.utp.edu.my/22082/1/BanSam_MSc_e-Thesis.pdf SAM, BAN (2017) NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE. Masters thesis, Universiti Teknologi PETRONAS.
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Electronic and Digitized Intellectual Asset
url_provider http://utpedia.utp.edu.my/
language English
topic TJ Mechanical engineering and machinery
spellingShingle TJ Mechanical engineering and machinery
SAM, BAN
NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE
description Oil and gas offshore production headers frequently experience random trips which is suspected to be due to liquid carryover issues as a result of sudden slug generation in the production headers. These slug generations are caused by sudden increase in gas velocity which provides sufficient drag to allow the free surface wave to grow on gasliquid interface to a height sufficient to bridge the pipe. This hydrodynamic slugging is difficult to predict since it can occur over a wide range of gas-liquid flow conditions. Compounding the complexity is the issue of no standard consensus of applicability of numerous operational correlations associated with slugging, e.g. pressure gradient, liquid holdup and slugging frequency. The objective of this study is to investigate oilgas slug formation in horizontal straight pipe and its associated pressure gradient, slug liquid holdup and slug frequency. The abrupt change in gas/liquid velocities, which causes transition of flow patterns was analyzed by using FLUENT 16.1. The incompressible Volume of Fluid (VOF) method was used to capture the transient distribution of segregated gas-liquid interface in different flow patterns. The validity of present model and its methodology was compared using Baker chart for 3.15 inches diameter horizontal pipe. The numerical solution was also compared quantitatively with existing experimental data to ensure its correctness. Finally, analyses were carried out for oil and gas vapor flow, covering substantial region of slug flow regime map. Concurrently, slug pressure gradient, liquid holdup and frequency were extracted numerically, and compared to existing empirical correlations. The present results compares favorably with some correlations and identified some outlier empirical models, which may not be suitable for operational usage.
format Thesis
author SAM, BAN
author_facet SAM, BAN
author_sort SAM, BAN
title NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE
title_short NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE
title_full NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE
title_fullStr NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE
title_full_unstemmed NUMERICAL SIMULATION OF TWO-PHASE SLUG FLOW REGIME IN HORIZONTAL PIPE
title_sort numerical simulation of two-phase slug flow regime in horizontal pipe
publishDate 2017
url http://utpedia.utp.edu.my/22082/1/BanSam_MSc_e-Thesis.pdf
http://utpedia.utp.edu.my/22082/
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score 13.160551