TY - GEN
T1 - Two-phase flow boiling heat transfer of R-22 and R-410A in horizontal microchannels
AU - Rifaldi, M.
AU - Pamitran, Agus Sunjarianto
AU - Choi, Kwang Il
AU - Oh, Jong Taek
AU - Hrnjak, Pega
PY - 2009
Y1 - 2009
N2 - Two-phase flow boiling heat transfer characteristics of R-22 and R-410A in horizontal small tubes was observed in this study. Heat flux over range of 10 to 40 kW m-2 was conducted to the test sections, which were made of stainless steel tube with inner tube diameters of 0.3, 0.5, 1.5 and 3.0 mm, and lengths of 0.27, 0.33, 1.5 and 3.0 m, respectively, to obtain the local heat transfer coefficients. Mass flux ran under range of 70 to 600 kg m-2 s-1, saturation temperature under range of 2 to 12°C, and quality under up to 1.0. The section was heated uniformly by applying an electric current to the tube directly. The effects of mass flux, heat flux, inner tube diameter and saturation temperature on heat transfer coefficient were presented. The heat transfer coefficients of the present study were compared using several existing heat transfer coefficient correlations. A new boiling heat transfer coefficient correlation based on the superposition model for refrigerants in small tubes, with considering the laminar flow, was developed.
AB - Two-phase flow boiling heat transfer characteristics of R-22 and R-410A in horizontal small tubes was observed in this study. Heat flux over range of 10 to 40 kW m-2 was conducted to the test sections, which were made of stainless steel tube with inner tube diameters of 0.3, 0.5, 1.5 and 3.0 mm, and lengths of 0.27, 0.33, 1.5 and 3.0 m, respectively, to obtain the local heat transfer coefficients. Mass flux ran under range of 70 to 600 kg m-2 s-1, saturation temperature under range of 2 to 12°C, and quality under up to 1.0. The section was heated uniformly by applying an electric current to the tube directly. The effects of mass flux, heat flux, inner tube diameter and saturation temperature on heat transfer coefficient were presented. The heat transfer coefficients of the present study were compared using several existing heat transfer coefficient correlations. A new boiling heat transfer coefficient correlation based on the superposition model for refrigerants in small tubes, with considering the laminar flow, was developed.
UR - http://www.scopus.com/inward/record.url?scp=84907416324&partnerID=8YFLogxK
M3 - Conference contribution
AN - SCOPUS:84907416324
SN - 9868509610
SN - 9789868509610
T3 - 4th Asian Conference on Refrigeration and Air-Conditioning, ACRA 2009
SP - 196
EP - 201
BT - 4th Asian Conference on Refrigeration and Air-Conditioning, ACRA 2009
PB - National Taipei University of Technology
T2 - 4th Asian Conference on Refrigeration and Air-Conditioning, ACRA 2009
Y2 - 20 May 2009 through 22 May 2009
ER -