Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel

Printed Circuit Heat Exchanger (PCHE) is considered as a promising heat exchanger for offshore Liquefied Natural Gas (LNG) production due to its compactness and high efficiency. To reveal the flow and heat transfer performance of real component nature gas mixture in PCHE, numerical study was conduct...

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Main Authors: Wang Yue, Li Yue, Chen Jie, Li Qian, Cai Weihua
Format: Article
Language:English
Published: EDP Sciences 2022-01-01
Series:Science and Technology for Energy Transition
Subjects:
Online Access:https://www.stet-review.org/articles/stet/full_html/2022/01/stet210268/stet210268.html
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author Wang Yue
Li Yue
Chen Jie
Li Qian
Cai Weihua
author_facet Wang Yue
Li Yue
Chen Jie
Li Qian
Cai Weihua
author_sort Wang Yue
collection DOAJ
description Printed Circuit Heat Exchanger (PCHE) is considered as a promising heat exchanger for offshore Liquefied Natural Gas (LNG) production due to its compactness and high efficiency. To reveal the flow and heat transfer performance of real component nature gas mixture in PCHE, numerical study was conducted to obtain flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel of PCHE. The influence of operating parameters including inlet temperature, mass flux and outlet pressure are investigated. The simulation results show that heat transfer coefficient and pressure drop increase with the increase of inlet temperature and mass flux, and decrease with the increase of outlet pressure. The overall variation tendency of heat transfer coefficient and pressure drop in supercritical methane–ethane mixture flow was similar to those in supercritical methane flow, but there still exists some difference due to their different physical properties. For the value of heat transfer coefficient, supercritical methane flow is about 7% larger than that of supercritical methane–ethane mixture flow. And for frictional pressure drop, supercritical methane flow is much larger by about 12%. Finally, new correlations were proposed for supercritical methane–ethane mixture flow, which are helpful for a more accurate flow and heat transfer calculation in PCHE designing for natural gas.
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spelling doaj.art-20b88153f7d3498d8e1a4dbf5ceefbef2022-12-22T03:38:15ZengEDP SciencesScience and Technology for Energy Transition2804-76992022-01-01771210.2516/stet/2022012stet210268Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channelWang Yue0Li Yue1Chen Jie2Li Qian3Cai Weihua4https://orcid.org/0000-0001-5614-428XLaboratory of Thermo-Fluid Science and Nuclear Engineering, Northeast Electric Power UniversityLaboratory of Thermo-Fluid Science and Nuclear Engineering, Northeast Electric Power UniversityCNOOC Gas and Power GroupLaboratory of Thermo-Fluid Science and Nuclear Engineering, Northeast Electric Power UniversityLaboratory of Thermo-Fluid Science and Nuclear Engineering, Northeast Electric Power UniversityPrinted Circuit Heat Exchanger (PCHE) is considered as a promising heat exchanger for offshore Liquefied Natural Gas (LNG) production due to its compactness and high efficiency. To reveal the flow and heat transfer performance of real component nature gas mixture in PCHE, numerical study was conducted to obtain flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel of PCHE. The influence of operating parameters including inlet temperature, mass flux and outlet pressure are investigated. The simulation results show that heat transfer coefficient and pressure drop increase with the increase of inlet temperature and mass flux, and decrease with the increase of outlet pressure. The overall variation tendency of heat transfer coefficient and pressure drop in supercritical methane–ethane mixture flow was similar to those in supercritical methane flow, but there still exists some difference due to their different physical properties. For the value of heat transfer coefficient, supercritical methane flow is about 7% larger than that of supercritical methane–ethane mixture flow. And for frictional pressure drop, supercritical methane flow is much larger by about 12%. Finally, new correlations were proposed for supercritical methane–ethane mixture flow, which are helpful for a more accurate flow and heat transfer calculation in PCHE designing for natural gas.https://www.stet-review.org/articles/stet/full_html/2022/01/stet210268/stet210268.htmlliquefied natural gassupercritical methane–ethane mixtureprinted circuit heat exchangerthermal performancenumerical simulation
spellingShingle Wang Yue
Li Yue
Chen Jie
Li Qian
Cai Weihua
Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel
Science and Technology for Energy Transition
liquefied natural gas
supercritical methane–ethane mixture
printed circuit heat exchanger
thermal performance
numerical simulation
title Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel
title_full Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel
title_fullStr Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel
title_full_unstemmed Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel
title_short Numerical investigation on flow and heat transfer characteristics of supercritical methane–ethane mixture in a straight channel
title_sort numerical investigation on flow and heat transfer characteristics of supercritical methane ethane mixture in a straight channel
topic liquefied natural gas
supercritical methane–ethane mixture
printed circuit heat exchanger
thermal performance
numerical simulation
url https://www.stet-review.org/articles/stet/full_html/2022/01/stet210268/stet210268.html
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