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
[21]  
Inoue N., 2000, ADV ENHANCED HEAT TR, V365, P23
[22]   Boiling heat transfer and flow characteristic of R32 inside a horizontal small-diameter microfin tube [J].
Jige, Daisuke ;
Sagawa, Kentaro ;
Iizuka, Shota ;
Inoue, Norihiro .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2018, 95 :73-82
[23]   A GENERAL CORRELATION FOR SATURATED 2-PHASE FLOW BOILING HEAT-TRANSFER INSIDE HORIZONTAL AND VERTICAL TUBES [J].
KANDLIKAR, SG .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1990, 112 (01) :219-228
[24]  
Kido O., 1995, ASMEJSME THERMAL ENG, V2, P323
[25]   Condensation heat transfer of R22 and R410A in horizontal smooth and microfin tubes [J].
Kim, MH ;
Shin, JS .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2005, 28 (06) :949-957
[26]   Evaporation Heat Transfer and Pressure Drop of R-410A in a 5.0mm O.D. Smooth and Microfin Tube [J].
Kim, Nae-Hyun .
INTERNATIONAL JOURNAL OF AIR-CONDITIONING AND REFRIGERATION, 2015, 23 (01)
[27]   Evaporation heat transfer and pressure drop of R-410A in three 7.0 mm OD microfin tubes having different inside geometries [J].
Kim, Nae-Hyun .
JOURNAL OF MECHANICAL SCIENCE AND TECHNOLOGY, 2015, 29 (08) :3519-3530
[28]   Evaporation heat transfer characteristics of R-410A in 7 and 9.52 mm smooth/micro-fin tubes [J].
Kim, Y ;
Seo, K ;
Chung, JT .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2002, 25 (06) :716-730
[29]  
Kline S.J., 1952, ASME Mechanical Engineering, V75, P3
[30]  
Koyama S., 1995, P ENG FDN C CONV FLO