Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
5016938 | International Journal of Refrigeration | 2017 | 40 Pages |
Abstract
For designing LNG spiral wound heat exchangers (SWHE), the boiling heat transfer mechanism of two-phase hydrocarbon refrigerant flowing downward in shell side should be known. In this study, an explosion-proof experimental rig was established for measuring heat transfer coefficients (HTC) and observing flow patterns. The test section contains three-layer tube bundles to emulate the actual structure and flow conditions of an SWHE. Propane as one main component of shell-side refrigerant is used as the tested fluid. The experimental conditions cover heat fluxes of 4~10âkWâ
mâ2, mass fluxes of 40~80âkg (m2â
s)â1 and vapor qualities of 0.2~1.0. The results indicate that HTC initially increases and then decreases with the increment of vapor quality, representing a maximum at a vapor quality of 0.8~0.9; the effect of heat flux on HTC increases with the increment of heat flux. A correlation of HTC was developed covering 98% of the experimental data within a deviation of ±20%.
Keywords
Related Topics
Physical Sciences and Engineering
Engineering
Mechanical Engineering
Authors
Chao Ding, Haitao Hu, Guoliang Ding, Jie Chen, Xiaoguang Mi, Sicong Yu, Jianrui Li,