Numerical simulation on deposition evolution of natural gas hydrate in pipeline

The traditional Euler-Euler fluid model is to predict the flow and deposition of two phases by approximating the hydrate particles as a fluid phase, but does not consider the effect of particle formation caused by phase change in the flow process. Herein, the Euler-Euler fluid mode, the interfacial...

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Main Authors: Xiang LIU, Wuchang WANG, Jialu ZHANG, Yuxing LI, Qihui HU, Yuanxing NING, Zhiming LIU
Format: Article
Language:zho
Published: Editorial Office of Oil & Gas Storage and Transportation 2022-02-01
Series:You-qi chuyun
Subjects:
Online Access:http://yqcy.xml-journal.net/cn/article/doi/10.6047/j.issn.1000-8241.2022.02.011
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author Xiang LIU
Wuchang WANG
Jialu ZHANG
Yuxing LI
Qihui HU
Yuanxing NING
Zhiming LIU
author_facet Xiang LIU
Wuchang WANG
Jialu ZHANG
Yuxing LI
Qihui HU
Yuanxing NING
Zhiming LIU
author_sort Xiang LIU
collection DOAJ
description The traditional Euler-Euler fluid model is to predict the flow and deposition of two phases by approximating the hydrate particles as a fluid phase, but does not consider the effect of particle formation caused by phase change in the flow process. Herein, the Euler-Euler fluid mode, the interfacial area transport equation and the convection equation were implanted into the open source computing software OpenFoam 4.0, and the key phase change source term was introduced with consideration to the hydrate particle aggregation and breakage efficiency. The amount of hydrate formation was calculated in real time according to the temperature field distribution in the pipeline and taken into account in the subsequent flow deposition process. However, the thermal insulation effect brought by the deposition in the pipeline will have an effect on the temperature field distribution, resulting in the dynamic evolution of the deposits. The numerical simulation results show that: the hydrates are firstly deposited on the top of the pipeline with the increase of hydrate volume fraction in the pipeline inlet, showing the trend of marginalization and centripetal growth. More hydrates will be formed in the system as the degree of supercooling increases continuously, but there is an obvious threshold for the maximum particle size. Among different flow modes, it is found that uniform flow is the safest flow condition in the pipeline. It can provide theoretical basis for the exploitation, prevention and control of deep-sea hydrate slurry.
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spelling doaj.art-defd963837454eee8831ff050986447b2024-04-13T02:28:16ZzhoEditorial Office of Oil & Gas Storage and TransportationYou-qi chuyun1000-82412022-02-0141221121810.6047/j.issn.1000-8241.2022.02.011yqcy-41-2-211Numerical simulation on deposition evolution of natural gas hydrate in pipelineXiang LIU0Wuchang WANG1Jialu ZHANG2Yuxing LI3Qihui HU4Yuanxing NING5Zhiming LIU6CNOOC Research Institute Co. Ltd.//State Key Laboratory of Natural Gas HydrateCollege of Pipeline and Civil Engineering, China University of Petroleum (East China)//Shangdong Key Laboratory of Oil & Gas Storage and Transportation SafetyCNOOC Research Institute Co. Ltd.//State Key Laboratory of Natural Gas HydrateCollege of Pipeline and Civil Engineering, China University of Petroleum (East China)//Shangdong Key Laboratory of Oil & Gas Storage and Transportation SafetyCNOOC Research Institute Co. Ltd.//State Key Laboratory of Natural Gas HydrateCNOOC Research Institute Co. Ltd.//State Key Laboratory of Natural Gas HydrateCNOOC Research Institute Co. Ltd.//State Key Laboratory of Natural Gas HydrateThe traditional Euler-Euler fluid model is to predict the flow and deposition of two phases by approximating the hydrate particles as a fluid phase, but does not consider the effect of particle formation caused by phase change in the flow process. Herein, the Euler-Euler fluid mode, the interfacial area transport equation and the convection equation were implanted into the open source computing software OpenFoam 4.0, and the key phase change source term was introduced with consideration to the hydrate particle aggregation and breakage efficiency. The amount of hydrate formation was calculated in real time according to the temperature field distribution in the pipeline and taken into account in the subsequent flow deposition process. However, the thermal insulation effect brought by the deposition in the pipeline will have an effect on the temperature field distribution, resulting in the dynamic evolution of the deposits. The numerical simulation results show that: the hydrates are firstly deposited on the top of the pipeline with the increase of hydrate volume fraction in the pipeline inlet, showing the trend of marginalization and centripetal growth. More hydrates will be formed in the system as the degree of supercooling increases continuously, but there is an obvious threshold for the maximum particle size. Among different flow modes, it is found that uniform flow is the safest flow condition in the pipeline. It can provide theoretical basis for the exploitation, prevention and control of deep-sea hydrate slurry.http://yqcy.xml-journal.net/cn/article/doi/10.6047/j.issn.1000-8241.2022.02.011deep-sea pipelinenatural gas hydrateinterfacial area transportphase changedeposition
spellingShingle Xiang LIU
Wuchang WANG
Jialu ZHANG
Yuxing LI
Qihui HU
Yuanxing NING
Zhiming LIU
Numerical simulation on deposition evolution of natural gas hydrate in pipeline
You-qi chuyun
deep-sea pipeline
natural gas hydrate
interfacial area transport
phase change
deposition
title Numerical simulation on deposition evolution of natural gas hydrate in pipeline
title_full Numerical simulation on deposition evolution of natural gas hydrate in pipeline
title_fullStr Numerical simulation on deposition evolution of natural gas hydrate in pipeline
title_full_unstemmed Numerical simulation on deposition evolution of natural gas hydrate in pipeline
title_short Numerical simulation on deposition evolution of natural gas hydrate in pipeline
title_sort numerical simulation on deposition evolution of natural gas hydrate in pipeline
topic deep-sea pipeline
natural gas hydrate
interfacial area transport
phase change
deposition
url http://yqcy.xml-journal.net/cn/article/doi/10.6047/j.issn.1000-8241.2022.02.011
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AT yuxingli numericalsimulationondepositionevolutionofnaturalgashydrateinpipeline
AT qihuihu numericalsimulationondepositionevolutionofnaturalgashydrateinpipeline
AT yuanxingning numericalsimulationondepositionevolutionofnaturalgashydrateinpipeline
AT zhimingliu numericalsimulationondepositionevolutionofnaturalgashydrateinpipeline