Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry

Two-phase flows are common occurrences in many industrial applications. The understanding of their characteristics in industrial piping systems is vital for the efficient design, optimization, and operation of industrial processes. Most of the previous experimental studies involving the use of gamma...

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Main Authors: Yahaya D. Baba, Joseph X.F. Ribeiro, Aliyu M. Aliyu, Archibong Archibong-Eso, Umar D. Abubakar, Adegboyega B. Ehinmowo
Format: Article
Language:English
Published: Elsevier 2020-11-01
Series:Scientific African
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S246822762030288X
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spelling doaj-965cc0f5c70d43b89986a19e2568b0972020-12-25T05:11:16ZengElsevierScientific African2468-22762020-11-0110e00550Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometryYahaya D. Baba0Joseph X.F. Ribeiro1Aliyu M. Aliyu2Archibong Archibong-Eso3Umar D. Abubakar4Adegboyega B. Ehinmowo5Department of Chemical and Biological Engineering, University of Sheffield, Sheffield S1 3JD, UKKumasi Technical University, P. O. Box 854, Kumasi, Ghana; Corresponding author.School of Computing &amp; Engineering, University of Huddersfield, Queensgate HD1 3DH, UKDepartment of Mechanical Engineering, University of Birmingham, Dubai, UAEDepartment of Civil Engineering, Kaduna Polytechnic, Kaduna State, NigeriaDepartment of Chemical and Petroleum Engineering, University of Lagos, Akoka, Lagos, Nigeria; Oil and Gas Engineering Centre, Cranfield University, Bedfordshire, MK43 0AL, UKTwo-phase flows are common occurrences in many industrial applications. The understanding of their characteristics in industrial piping systems is vital for the efficient design, optimization, and operation of industrial processes. Most of the previous experimental studies involving the use of gamma densitometers for holdup measurements in air-water mixtures are limited to smaller diameter pipes (generally regarded as those with < 50 mm in nominal diameter). Further, very few literature report experimental data obtained using gamma desitometers. This paper presents an application of a gamma densitometer in the measurement of two-phase flow characteristics in an intermediate diameter pipe (nominal diameter between 50 mm and 100 mm). Scaled air-water experiments were performed in a 17-m long, 0.0764-m internal diameter horizontal pipe. Liquid superficial velocity ranged between 0.1–0.4 m/s while gas superficial velocity ranged from 0.3 to 10.0 m/s. The measured parameters include liquid holdup, pressure gradient, flow pattern, and slug flow features. The flow patterns observed were stratified, stratified-wavy, plug, slug, and annular flows. Plug and slug flow patterns showed good agreement with established flow pattern maps. Furthermore, the slug translational velocity was observed to increase with increasing mixture velocity, as reported by previous authors, hence establishing the reliability of the instrumentation employed. The slug body length was also measured using the gamma densitometer and was found to be within the range 24–36D with a mean length of 30.6D.http://www.sciencedirect.com/science/article/pii/S246822762030288XTwo-phase flowGamma densitometryPressure gradientLiquid holdup and Slug flow
collection DOAJ
language English
format Article
sources DOAJ
author Yahaya D. Baba
Joseph X.F. Ribeiro
Aliyu M. Aliyu
Archibong Archibong-Eso
Umar D. Abubakar
Adegboyega B. Ehinmowo
spellingShingle Yahaya D. Baba
Joseph X.F. Ribeiro
Aliyu M. Aliyu
Archibong Archibong-Eso
Umar D. Abubakar
Adegboyega B. Ehinmowo
Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry
Scientific African
Two-phase flow
Gamma densitometry
Pressure gradient
Liquid holdup and Slug flow
author_facet Yahaya D. Baba
Joseph X.F. Ribeiro
Aliyu M. Aliyu
Archibong Archibong-Eso
Umar D. Abubakar
Adegboyega B. Ehinmowo
author_sort Yahaya D. Baba
title Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry
title_short Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry
title_full Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry
title_fullStr Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry
title_full_unstemmed Characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry
title_sort characteristics of horizontal gas-liquid two-phase flow measurement in a medium-sized pipe using gamma densitometry
publisher Elsevier
series Scientific African
issn 2468-2276
publishDate 2020-11-01
description Two-phase flows are common occurrences in many industrial applications. The understanding of their characteristics in industrial piping systems is vital for the efficient design, optimization, and operation of industrial processes. Most of the previous experimental studies involving the use of gamma densitometers for holdup measurements in air-water mixtures are limited to smaller diameter pipes (generally regarded as those with < 50 mm in nominal diameter). Further, very few literature report experimental data obtained using gamma desitometers. This paper presents an application of a gamma densitometer in the measurement of two-phase flow characteristics in an intermediate diameter pipe (nominal diameter between 50 mm and 100 mm). Scaled air-water experiments were performed in a 17-m long, 0.0764-m internal diameter horizontal pipe. Liquid superficial velocity ranged between 0.1–0.4 m/s while gas superficial velocity ranged from 0.3 to 10.0 m/s. The measured parameters include liquid holdup, pressure gradient, flow pattern, and slug flow features. The flow patterns observed were stratified, stratified-wavy, plug, slug, and annular flows. Plug and slug flow patterns showed good agreement with established flow pattern maps. Furthermore, the slug translational velocity was observed to increase with increasing mixture velocity, as reported by previous authors, hence establishing the reliability of the instrumentation employed. The slug body length was also measured using the gamma densitometer and was found to be within the range 24–36D with a mean length of 30.6D.
topic Two-phase flow
Gamma densitometry
Pressure gradient
Liquid holdup and Slug flow
url http://www.sciencedirect.com/science/article/pii/S246822762030288X
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