Gas-liquid two phase flow heat transfer at high subcooling in vertical tube
|更新时间:2025-12-10
|
Gas-liquid two phase flow heat transfer at high subcooling in vertical tube
CIESC JournalIssue 9, Pages: 2314-2319(2010)
作者机构:
中国石油大学化工学院
作者简介:
基金信息:
DOI:
CLC:
Online First:05 September 2010,
Published:05 September 2010
稿件说明:
移动端阅览
DOU Congcong, MAO Yu, WANG Juan, et al. Gas-liquid two phase flow heat transfer at high subcooling in vertical tube[J]. CIESC Journal, 2010, (9): 2314-2319.
DOI:
DOU Congcong, MAO Yu, WANG Juan, et al. Gas-liquid two phase flow heat transfer at high subcooling in vertical tube[J]. CIESC Journal, 2010, (9): 2314-2319.DOI:
Gas-liquid two phase flow heat transfer at high subcooling in vertical tube
Subcooled boiling model suitable for high pressure and high subcooling condition was established based on two-fluid model.The influence of liquid subcooling and wall heat flux on heat characteristics was investigated.The results show that distribution of gas phase throughout the cross section is nonuniform,and bubbles are intensive near the wall.The volume fraction increases with decreasing entrance subcooling which prompts the boiling heat transfer.With increasing heat flux,the surface heat transfer coefficient generally increases along the axial direction,however,decreasing tendency can be observed in local area,which becomes unclear with decreasing entrance subcooling.