Evaporation flow pattern and heat transfer of R-22 and R-134a in small diameter tubes

被引:51
作者
Oh, Hoo-Kyu [1 ]
Son, Chang-Hyo [1 ]
机构
[1] Pukyong Natl Univ, Coll Engn, Dept Refrigerat & Air Conditioning Engn, Pusan 608739, South Korea
关键词
PRESSURE-DROP; 2-PHASE FLOW; GENERAL CORRELATION; CONDENSATION; PASSAGES; R410A; WATER; R134A; FLUX;
D O I
10.1007/s00231-011-0761-4
中图分类号
O414.1 [热力学];
学科分类号
摘要
The flow patterns and heat transfer coefficients of R-22 and R-134a during evaporation in small diameter tubes were investigated experimentally. The evaporation flow patterns of R-22 and R-134a were observed in Pyrex sight glass tubes with 2 and 8 mm diameter tube, and heat transfer coefficients were measured in smooth and horizontal copper tubes with 1.77, 3.36 and 5.35 mm diameter tube, respectively. In the flow patterns during evaporation process, the annular flows in 2 mm glass tube occurred at a relatively lower vapor quality compared to 8 mm glass tube. The flow patterns in 2 mm glass tube did not agree with the Mandhane's flow pattern maps. The evaporation heat transfer coefficients in the small diameter tubes (d (i) < 6 mm) were observed to be strongly affected by tube diameters, and to differ from those in the large diameter tubes. The heat transfer coefficients of 1.77 mm tube were higher than those of 3.36 mm and 5.35 mm tube. Most of the existing correlations failed to predict the evaporation heat transfer coefficient in small diameter tubes. Therefore, based on the experimental data, the new correlation is proposed to predict the evaporation heat transfer coefficients of R-22 and R-134a in small diameter tubes.
引用
收藏
页码:703 / 717
页数:15
相关论文
共 47 条
[1]   Vertical flow boiling of refrigerant R134a in small channels [J].
Agostini, B ;
Bontemps, A .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2005, 26 (02) :296-306
[2]  
Baker O., 1954, Oil and Gas Journal, V53, P185, DOI DOI 10.2118/323-G
[3]   Flow boiling heat transfer of Freon R11 and HCFC123 in narrow passages [J].
Bao, ZY ;
Fletcher, DF ;
Haynes, BS .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2000, 43 (18) :3347-3358
[4]  
BENNETT AW, 1966, P I MECH ENG 3C, V184, P260
[5]   CRITICAL-HEAT-FLUX AND FLOW-PATTERN OBSERVATIONS FOR LOW-PRESSURE WATER FLOWING IN TUBES [J].
BERGLES, AE ;
LOPINA, RF ;
FIORI, MP .
JOURNAL OF HEAT TRANSFER, 1967, 89 (01) :69-&
[6]   PREDICTION OF HORIZONTAL TUBESIDE CONDENSATION OF PURE COMPONENTS USING FLOW REGIME CRITERIA [J].
BREBER, G ;
PALEN, JW ;
TABOREK, J .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1980, 102 (03) :471-476
[7]   Two-phase frictional pressure gradient of R236ea, R134a and R410A inside multi-port mini-channels [J].
Cavallini, A ;
Del Col, D ;
Doretti, L ;
Matkovic, M ;
Rossetto, L ;
Zilio, C .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2005, 29 (07) :861-870
[8]   CORRELATION FOR BOILING HEAT TRANSFER TO SATURATED FLUIDS IN CONVECTIVE FLOW [J].
CHEN, JC .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1966, 5 (03) :322-&
[9]   Boiling heat transfer of R-22, R-134a, and CO2 in horizontal smooth minichannels [J].
Choi, Kwang-Il ;
Pamitran, A. S. ;
Oh, Chun-Young ;
Oh, Jong-Taek .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2007, 30 (08) :1336-1346
[10]   Two-phase pressure drop of R-410A in horizontal smooth minichannels [J].
Choi, Kwang-Il ;
Pamitran, A. S. ;
Oh, Chun-Young ;
Oh, Jong-Taek .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2008, 31 (01) :119-129