The topic of hydrate formation and blocking in offshore petroleum industry has attracted more and more attentions, which is known as one of the flow assurance issues. A new technology has been proposed to avoid the occurrence of hydrate blockage in multiphase transportation system, which is hydrate slurry flow technology, also named as cold flow technology. The low dosage hydrate inhibitor of anti-agglomerate was added into the flow systems to allow hydrate formation in the liquid phase while it prevented the aggregation of hydrate particles. Thus these particles were evacuated with the liquid phase as pseudo-fluid like slurry. In this work, an inward and outward hydrate growth shell model coupled with two phase flow hydrodynamic model was applied to investigate the characteristics of gas-hydrate slurry stratified flow. The inward and outward hydrate growth shell model considered the kinetics, mass transfer and heat transfer process of hydrate formation, which could predict the hydrate formation rate and the released heat. The two phase flow hydrodynamic model included mass, momentum and energy equations. A case for an inclined pipeline was simulated using the combined models. The results showed that once the kinetic requirements for hydrate crystallization was satisfied, hydrates would form quickly at the initial stage and then hydrate formation rate would decrease obviously due to the limitation of mass transfer and heat transfer. Meanwhile, the flow characteristics, such as the liquid holdup and pressure drop, were predicted by the model, which also provided an acceptable results about the state of hydrates (onset time of formation, formation rate, volume fraction, etc.) in multiphase system for the operation engineers in the field. The key parameters of the inward and outward hydrate growth shell model were determined by referring to the literatures. To investigate the reliability and influence of these set values on the results, a sensitivity analysis of the key parameters of the shell model was implemented. Further works should be done, such as the flow mechanism in other flow regimes as well as the influence of particle aggregation.
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2016 11th International Pipeline Conference
September 26–30, 2016
Calgary, Alberta, Canada
Conference Sponsors:
- Pipeline Division
ISBN:
978-0-7918-5026-8
PROCEEDINGS PAPER
Simulation of Gas-Hydrate Slurry Stratified Flow With Inward and Outward Hydrate Growth Model
Bohui Shi,
Bohui Shi
China University of Petroleum-Beijing, Beijing, China
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Yang Liu,
Yang Liu
China University of Petroleum-Beijing, Beijing, China
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Lin Ding,
Lin Ding
China University of Petroleum-Beijing, Beijing, China
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Xiaofang Lv,
Xiaofang Lv
Chang Zhou University, Changzhou, China
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Jing Gong
Jing Gong
China University of Petroleum-Beijing, Beijing, China
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Bohui Shi
China University of Petroleum-Beijing, Beijing, China
Yang Liu
China University of Petroleum-Beijing, Beijing, China
Lin Ding
China University of Petroleum-Beijing, Beijing, China
Xiaofang Lv
Chang Zhou University, Changzhou, China
Jing Gong
China University of Petroleum-Beijing, Beijing, China
Paper No:
IPC2016-64303, V002T08A004; 11 pages
Published Online:
November 10, 2016
Citation
Shi, B, Liu, Y, Ding, L, Lv, X, & Gong, J. "Simulation of Gas-Hydrate Slurry Stratified Flow With Inward and Outward Hydrate Growth Model." Proceedings of the 2016 11th International Pipeline Conference. Volume 2: Pipeline Safety Management Systems; Project Management, Design, Construction and Environmental Issues; Strain Based Design; Risk and Reliability; Northern Offshore and Production Pipelines. Calgary, Alberta, Canada. September 26–30, 2016. V002T08A004. ASME. https://doi.org/10.1115/IPC2016-64303
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