Convective boiling of R-410A in 5.0 and 7.0 mm outer diameter microfin tubes

被引:4
作者
Kim, Nae-Hyun [1 ]
机构
[1] Incheon Natl Univ, Dept Mech Engn, Incheon 22012, South Korea
关键词
Evaporation; flow boiling; R-410A; microfin; heat transfer; pressure drop; small diameter; EVAPORATION HEAT-TRANSFER; FRICTIONAL PRESSURE-DROP; GENERAL CORRELATION; HORIZONTAL TUBES; PART II; REFRIGERANTS; CONDENSATION; SMOOTH; R410A; MODEL;
D O I
10.1080/08916152.2019.1641168
中图分类号
O414.1 [热力学];
学科分类号
摘要
Although microfin tubes are widely used in refrigeration and air-conditioning industries, relatively little data are available for small diameter tubes. In the present study, 7.0 and 5.0 mm outer diameter (O.D.) microfin tubes were tested for a range of mass flux (from 50 to 250 kg/m(2)s) and vapor quality (from 0.2 to 0.8). The saturation temperature was 8 degrees C and the heat flux was 3.0 kW/m(2). This heat flux is quite small, and existing investigations have not been gone to this low heat flux. Results showed that an optimum behavior was observed for the enhancement factor. It increased as mass flux increased up to 150 kg/m(2)s, and then decreased with a further increase of mass flux. The penalty factors were larger than 1.0 except at the lowest mass flux of 50 kg/m(2)s. Possible reasoning was provided based on flow patterns of the microfin and the smooth tube. The enhancement factor ranged from 1.24 to 1.93 for the 7.0 mm microfin tube, and 1.63 to 3.26 for the 5.0 mm microfin tube. The penalty factor ranged from 0.82 to 1.11 and from 0.48 to 1.39 for the 7.0 mm and the 5.0 mm microfin tube, respectively. Larger high fin height of the 5.0 mm microfin tube may be responsible for the larger enhancement and penalty factor of the 5.0 mm microfin tube. Comparison with predictions by existing correlations revealed that 7.0 mm microfin tube data were reasonably predicted. However, 5.0 mm microfin tube data were generally underpredicted, probably due to the large fin height of the 5.0 mm microfin tube.
引用
收藏
页码:355 / 373
页数:19
相关论文
共 45 条
[1]  
[Anonymous], **NON-TRADITIONAL**
[2]   In-tube evaporation and condensation of R-22 and R-410A with plain and internally enhanced tubes [J].
Bogart, J ;
Thors, P .
JOURNAL OF ENHANCED HEAT TRANSFER, 1999, 6 (01) :37-50
[3]  
Cavallini A., 2006, P 6 ECI INT C BOIL H
[4]  
CAVALLINI A, 1997, HEAT TECHNOLOGY, V15, P3
[5]  
Cavallini A., 1999, HEAT TECHNOLOGY, V17, P29
[6]   Investigation of boiling heat transfer characteristics of R134a flowing in smooth and microfin tubes [J].
Celen, Ali ;
Cebi, Alican ;
Dalkilic, Ahmet Selim .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2018, 93 :21-33
[7]   Modelling of evaporation heat transfer of pure refrigerants and refrigerant mixtures in microfin tubes [J].
Charnra, L. M. ;
Mago, P. J. .
PROCEEDINGS OF THE INSTITUTION OF MECHANICAL ENGINEERS PART C-JOURNAL OF MECHANICAL ENGINEERING SCIENCE, 2007, 221 (04) :443-454
[8]  
Choi J.Y., 2001, Proc. IIF-IIR Comm. B1, V5, P9
[9]  
Collier J. G., 2004, ENG DATA BOOK
[10]  
Collier JR Thome J.G., 1996, Convective Boiling and Condensation