Experimental Investigation on the Condensation and Boiling Heat Transfer Performance of Refrigerant R245fa Outside Horizontal Stainless Steel Enhanced Tubes
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Experimental Investigation on the Condensation and Boiling Heat Transfer Performance of Refrigerant R245fa Outside Horizontal Stainless Steel Enhanced Tubes
Journal of Xi'an Jiaotong UniversityVol. 60, Issue 4, Pages: 218-226(2026)
JIANG Dong, CHEN Man, ZHANG Fu, et al. Experimental Investigation on the Condensation and Boiling Heat Transfer Performance of Refrigerant R245fa Outside Horizontal Stainless Steel Enhanced Tubes[J]. Journal of Xi'an Jiaotong University, 2026, 60(4): 218-226.
DOI:
JIANG Dong, CHEN Man, ZHANG Fu, et al. Experimental Investigation on the Condensation and Boiling Heat Transfer Performance of Refrigerant R245fa Outside Horizontal Stainless Steel Enhanced Tubes[J]. Journal of Xi'an Jiaotong University, 2026, 60(4): 218-226.DOI: 10.7652/xjtuxb202604018.
Experimental Investigation on the Condensation and Boiling Heat Transfer Performance of Refrigerant R245fa Outside Horizontal Stainless Steel Enhanced Tubes
To address the issue of low heat transfer efficiency of refrigerant R245fa in high-temperature heat pump and organic Rankin
e cycle systems,an experimental study on its condensation and boiling heat transfer performance outside 304 stainless steel tubes was conducted.Two enhanced condensation tubes(two-dimensional tube C1 and three-dimensional tube C2)and two enhanced boiling tubes(boiling tube E1 and T-type boiling tube E2)were selected as test subj ects.The influence of different tube structures on the enhanced phase-change heat transfer performance of stainless steel tubes was investigated under a condensation temperature of 50 ℃ and an evaporation temperature of 30℃.The results indicate that for the tubes with better heat transfer performance(the three-dimensional condensation tube C2 and the T-type boiling tube E2),the overall heat transfer coefficients range from 2500 to 3200 W/(m
2
·K)at a flow velocity of 1.0—4.0 m/s and a heat flux density of 20 kW/m
2
.The thermal resistance of the tube wall accounts for 30%—40% of the total thermal resistance.The external fin structure of the stainless steel tubes significantly affects the condensation and boiling heat transfer performance. Both the three-dimensional condensation tube C2 and the T-type boiling tube E2 exhibit superior heat transfer performance. Compared to tube C1,the overall and external heat transfer coefficients of tube C2 are 5%—7% and 3%—8% higher,respectively.Similarly,compared to tube E1,the overall and external heat transfer coefficients of tube E2 are 22%—32% and 27%—38% higher,respectively.This study provides important references for the design and optimization of evaporators and condensers in high-temperature heat pump and organic Rankine cycle systems,contributing to the improvement of heat transfer efficiency and overall system performance.
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