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Heat Transfer Characteristics During Gas Cooling Process of Carbon Dioxide in a Horizontal Tube

수평관내 초임계 영역의 Co2 냉각 열전달 특성

  • 손창효 (부경대학교 대학원 냉동공학과) ;
  • 이동건 (부경대학교 대학원 냉동공학과) ;
  • 오후규 (부경대학교 냉동공조공학과) ;
  • 정시영 (서강대학교 기계공학부) ;
  • 김영률 (한국생산기술연구원)
  • Published : 2004.03.01

Abstract

The heat transfer coefficient and pressure drop during gas cooling process of carbon dioxide in a horizontal tube were investigated. The experiments were conducted without oil in the refrigerant loop. The main components of the refrigerant loop are a receiver, a variable-speed pump, a mass flowmeter, an evaporator, and a gas cooler(test section). The main components of the water loop consist of a variable-speed pump, an isothermal tank, and a flowmeter. The gas cooler is a counterflow heat exchanger with refrigerant flowing in the inner tube and water flowing in the annulus. The test section consists of smooth, horizontal stainless steel tube of the outer diameter of 9.53mm and of the inner diameter of 7.75mm. The length of the test section is 6m. The refrigerant mass fluxes were 200∼300kg/(m2$.$s) and the inlet pressure of the gas cooler varied from 7.5㎫ to 8.5㎫. The main results were summarized as follows : Pressure drop of CO2 increases with increasing gas cooler pressure. The friction factors of CO2 in a horizontal tube show a relatively good agreement with the correlation by Blasius. The heat transfer coefficient of CO2 in transcritical region increases with decreasing gas cooler pressure and decreasing mass flux of CO2. Most of correlations proposed in a transcritical region showed significant deviations with experimental data except for those predicted by Gnielinski.

Keywords

References

  1. Boewe DE, Yin JM, Park YC, Bullard CW, and Hrnjak PS., 1999, 'The Role of Suction Line Heat Exchanger in Transcritical R-744 Mobile A/C Systems,' SAE International Congress and Exposition, Detroit, Michigan, Paper No. 1999-01-0583
  2. Hashimoto K, Saikawa M and Iwatsubo T., 2000, 'Experimental Study About Heat Transfer Coefficient of $CO_2$ on Supercritical Condition,' The 34th of Heat Transfer Symposium of Japan, pp. 401-402
  3. Kruse H, Heidelck R and Suss J., 1999, The Application of $CO_2$ as a Refrigerant,' Bulletin of the International Institute of Refrigeration, 99-1:2-21
  4. Pettersen J, Rieberer R and Munkejord ST., 2000, 'Heat Transfer and Pressure Drop for Flow of Supercritical and Subcritical $CO_2$ in Microchannel Tubes,' SINTEF Energy Research
  5. Preessner M, Culter B, Singanamalla S, Hwang Y and Radermacher R, 2000, 'Comparison of Automotive Air Conditioning Systems Operating with $CO_2$ and R-134a,' in Proceedings of 4th IIR-Gustav Lorentzen Conference on Natural Working Fluids at Purdue, West Lafayette, Indiana, 185-192
  6. Koji Mori, Junji Onishi, Hirokazu Shimaoka, Shigeyasu Nakanishi and Hideo Kimoto, 2002, 'Cooling Heat Transfer Characteristics of $CO_2$ Oil Mixture at Spercritical Pressure Conditions,' Proceedings of the Asian Conference on Refrigeration and Air Conditioning, December 4, Kobe, Japan, pp. 81-86
  7. Dittus, F. W., and L. M. K. Boelter, 1930, University of California, Berkeley, Publications on Engineering, Vol. 2, p. 443
  8. Gnielinski, V., 1976, 'New Equations for Heat and Mass Transfer in Turbulent Pipe and Channel Flow,' Int. Chem. Eng. Vol. 16, pp. 359-368
  9. Petukhov, B. S., E. A. Krasnoshchekov, and V. S. Protopopov., 1961, 'An Investigation of Heat Transfer to Fluids Flowing in Pipes Under Supercritical Conditions,' ASME International Developments in Heat Transfer Part. 3, 569-578
  10. Pitla, S. S., Groll, E. A. and Ramadhyani, S., 2002, 'New Correlation to Predict the Heat Transfer Coefficient During In-Tube Cooling of Turbulent Supercritical $CO_2$.' International Journal of Refrigeration, Vol. 25, pp. 887-895 https://doi.org/10.1016/S0140-7007(01)00098-6
  11. Krasonshchekov, E. A., I. V. Kuraeva, and V. S. Protopopov., 1970, 'Local Heat transfer of Carbon Dioxide at Supercritical Pressure Under Cooling Conditions,' Teplofizika Vysokikh Temperatur, 7(5), 922-930
  12. Baskov, V. L., I. V. Kuraeva, and V. S. Protopopov., 1977, 'Heat Transfer With the Turbulent Flow of a Liquid at Supercritical Pressure in Tubes Under Cooling Conditions.,' Teplofizika Vysokikh Temperatur 15(1): 96-102
  13. Petrov, N. E. and V. N. Popov., 1985, 'Heat Transfer and Resistance of Carbon Being Cooled in the Supercritical Region,' Thermal Engineering., 32(3), 131-134
  14. Lei Gao and Tomohiro Honda, 2002, 'Experimental on Heat Transfer Characteristics of Heat Exchanger for $CO_2$ Heat Pump System,' Proceedings of the Asian Conference on Refrigeration and Air Conditioning, December 4, Kobe, Japan, pp. 75-80

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