TY - JOUR
T1 - Refrigerant distribution in horizontal headers with downward minichannel-branching conduits
T2 - Experiment, empirical correlation and two-phase flow pattern map
AU - Wijayanta, Agung Tri
AU - Miyazaki, Takahiko
AU - Koyama, Shigeru
N1 - Funding Information:
The financial assistance partially provided by Calsonic Kansei Corporation is gratefully acknowledged. The deep appreciation goes to Dr. Shirou Ikuta from Calsonic Kansei Corporation for his valuable comments in some discussions. The authors wish to thank their former colleagues, Dr. Ken Kuwahara, Dr. Nobuo Takata and Mr. Hiroaki Miyazaki, for their assistance during the experiments.
Publisher Copyright:
© 2016 Elsevier Inc.
PY - 2017/2/1
Y1 - 2017/2/1
N2 - The system energy efficiency will decline with the decrease of evaporator capacity because the use of more branches in evaporators increases maldistribution. This paper presents experimental study of several design options for downward flow to reduce the maldistribution. Two-phase flow distribution in a header type evaporator applied for CO2 have been experimentally investigated because the refrigeration system based on carbon dioxide (CO2) as a refrigerant is near ideal. Since the CO2 system works around critical pressure, an alternative method to predict the flow distribution of CO2 header type evaporator is inevitable. R134a is used as the alternative working fluid in the present study. Similarity hypothesis between CO2 and R134a is applied (refer to Wijayanta et al., 2016). R134a headers are tested and the experimental work is applicable to CO2. The R134a experiments were conducted at saturation temperature of about 21 °C, refrigerant mass flow range between 10 and 30 kg/h which corresponds to about 44 and 130 kg/m2 s in the 9 mm i.d. header, and average vapor quality in the test section inlet of about 0.1–0.4. The test section consists of a horizontal header with 3 and 6 vertically downward replaceable branching conduits. The vapor-liquid phase mass flows enter into the branches are measured to propose the configuration of the header that has the minimum maldistribution. Empirical correlation of the vapor-liquid distribution is developed. Estimated CO2 distribution for the proper header is determined based on R134a experimental data using the similarity hypothesis. The developed flow pattern map for R134a and CO2 is also proposed.
AB - The system energy efficiency will decline with the decrease of evaporator capacity because the use of more branches in evaporators increases maldistribution. This paper presents experimental study of several design options for downward flow to reduce the maldistribution. Two-phase flow distribution in a header type evaporator applied for CO2 have been experimentally investigated because the refrigeration system based on carbon dioxide (CO2) as a refrigerant is near ideal. Since the CO2 system works around critical pressure, an alternative method to predict the flow distribution of CO2 header type evaporator is inevitable. R134a is used as the alternative working fluid in the present study. Similarity hypothesis between CO2 and R134a is applied (refer to Wijayanta et al., 2016). R134a headers are tested and the experimental work is applicable to CO2. The R134a experiments were conducted at saturation temperature of about 21 °C, refrigerant mass flow range between 10 and 30 kg/h which corresponds to about 44 and 130 kg/m2 s in the 9 mm i.d. header, and average vapor quality in the test section inlet of about 0.1–0.4. The test section consists of a horizontal header with 3 and 6 vertically downward replaceable branching conduits. The vapor-liquid phase mass flows enter into the branches are measured to propose the configuration of the header that has the minimum maldistribution. Empirical correlation of the vapor-liquid distribution is developed. Estimated CO2 distribution for the proper header is determined based on R134a experimental data using the similarity hypothesis. The developed flow pattern map for R134a and CO2 is also proposed.
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U2 - 10.1016/j.expthermflusci.2016.09.011
DO - 10.1016/j.expthermflusci.2016.09.011
M3 - Article
AN - SCOPUS:84995896949
SN - 0894-1777
VL - 81
SP - 430
EP - 444
JO - Experimental Thermal and Fluid Science
JF - Experimental Thermal and Fluid Science
ER -