DOI QR코드

DOI QR Code

An Experimental Study on Heat Transfer and Pressure Drop Characteristics of Carbon Dioxide During Gas Cooling Process in a Hellically Coiled Tube

  • Oh, Hoo-Kyu (Pukyong National University, Dept. of Mechanical Engineering) ;
  • Son, Chang-Hyo (Pukyong National University, Dept. of Mechanical Engineering) ;
  • Yu, Tae-Geun (Pukyong National University, Dept. of Mechanical Engineering) ;
  • Kim, Dae-Hui (Samsung Electronics co ltd., System Appliance Division)
  • Published : 2007.05.31

Abstract

The heat transfer coefficient and pressure drop during 9as cooling process of $CO_2$ (R744) in a helically coiled copper tube with the inner diameter of 4.55 mm and outer diameter of 6.35 mm were investigated experimentally. The main components of the refrigerant loop are a receiver, a variable-speed pump. a mass flow meter a pre-heater and a helically coiled type gas cooler (test section). The refrigerant mass fluxes are varied from 200 to $800kg/m^2s$ and the inlet pressures of gas cooler are 7.5 to 10.0 MPa. The heat transfer coefficients of $CO_2$ in a helically coiled tube are higher than those in a horizontal tube. The Pressure drop of $CO_2$ in the gas cooler shows a relatively good agreement with those predicted by Ito's correlation developed for single-phase in a helically coiled tube. The local heat transfer coefficient of $CO_2$ agrees well with the correlation by Pitla et al. However. at the region near pseudo-critical temperature. the experiments indicate higher values than the Pitla et al correlation. Therefore, various experiments in helically coiled tubes have to be conducted and it is necessary to develop the reliable and accurate prediction determining the heat transfer and pressure drop of $CO_2$ in a helically coiled tube.

Keywords

References

  1. Lorentzen G, Pettersen J. 1993, A new, efficient and environmentally benign system for car air-conditioning, International Journal of Refrigeration, Vol. 16, No. 1, pp. 4-12 https://doi.org/10.1016/0140-7007(93)90014-Y
  2. Pettersen et al. 2000, Heat transfer and pressure drop for flow of supercritical and subcritical $CO_2$ in microchannel tubes : SINTEF Energy Research. G. S. Choi and C. S. Kim, Linear Stable Systems, 1993, IEEE Trans. of Automatic Control, Vol. 33, No. 3, pp. 1234-1245
  3. White C. M., Fluid friction and its relation to heat transfer, Trans. Inst. Chem. Engrs, Lond., 10 : pp. 66-80
  4. H. Ito, 1959, Frictional factors for turbulent flow in curved pipes, J. Eng., Vol. 81, pp. 123-134
  5. P. S. Srinivasan, S. S. Nandapurkar, F. A. Holland, 1968, Pressure drop and heat transfer in coils, Chem. Eng. 218, pp. 113-119
  6. Bringer R. P. And Smith J. M., 1957, AICHE. Journal, Vol. 3, No. 1, pp. 49-55 https://doi.org/10.1002/aic.690030110
  7. 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, pp. 569-578
  8. Petrov N. E. and Popov V. N., 1985, Heat Transfer and Resistance of Carbon Being Cooled in the Supercritical Region, Thermal Engineering, Vol. 32, No. 3, pp. 131-134
  9. Gnielinski V., 1976, New Equation for Heat and Mass Transfer in Turbulent Pipe and Channel Flow, Int. Chem. Eng., Vol. 16, pp. 359-368
  10. Pitla, S. S., Robinson, D. M., Groll, E. A. and Ramadhyani, S., 1998, Heat Transfer from Supercritical Carbon Dioxide in Tube Flow: A Critical Review, 1998, HVAC&R research, Vol. 4, No. 4, 281-301 https://doi.org/10.1080/10789669.1998.10391405
  11. Fang, X., Bullard, C. W., and Hrnjak, P. S., Heat Transfer and Pressure Drop of Gas Coolers, ASHRAE Transaction, Vol. 107, Part 1, pp. 255-266

Cited by

  1. Gas Cooler(2) - Experiments and Predictions on Heat Flowrate and Pressure Drop - vol.34, pp.2, 2010, https://doi.org/10.5916/jkosme.2010.34.2.259