Vapor-Liquid Equilibria of Carbon Dioxide and Propane Mixtures

이산화탄소와 프로판 혼합냉매의 기상-액상 평형

  • Kim, Ju-Hyok (School of Mechanical and Aerospace Engineering, Seoul National University) ;
  • Kim, Min-Soo (School of Mechanical and Aerospace Engineering, Seoul National University) ;
  • Kim, Man-Hoe (Department of Mechanical Engineering, KAIST)
  • 김주혁 (서울대학교 기계항공공학부) ;
  • 김민수 (서울대학교 기계항공공학부) ;
  • 김만회 (한국과학기술원 기계공학과)
  • Published : 2006.11.10

Abstract

This paper presents the vapor-liquid equilibrium (VLE) data measured for carbon dioxide and propane mixtures. Their mixtures were considered as promising alternative refrigerants due to good thermophysical properties and negligible environmental impact. The isothermal VLE data were measured at eight temperatures ranging from 253.15 to 323.15 K in the circulation type equipment with a view cell. The binary system was found to be a zeotropic mixture in the tested temperature range and could be correlated with sufficient accuracy by using the Peng-Robinson equation of state (PR EoS) with the van der Waals one fluid mixing rule. A comparison with published experimental VLE data has been carried out by means of the PR equation of state. In addition, the phase behaviors of carbon dioxide and propane mixtures were analyzed based on the measured VLE data.

Keywords

References

  1. Lemmon, E. W., McLinden, M. O. and Huber, M. L., 2002, Reference Fluid Thermodynamic and Transport Properties (REFPROP), NIST Standard Reference Database 23, Version 7.0, National Institute of Standards and Technology; Gaithersburg, Maryland, USA
  2. IPCC Third Assessment Report - Climate Change 2001
  3. Peng, D. Y and Robinson, D. B., 1976, A new two-constant equation of state, Ind. Eng. Chem. Fundarn., Vol. 15, pp.59-64 https://doi.org/10.1021/i160057a011
  4. Reamer, H. H., Sage, B. H. and Lacey, W. N., 1951, Phase equilibria in hydrocarbon systems, Ind. Eng. Chem., Vol. 43, pp.2515-2520 https://doi.org/10.1021/ie50503a035
  5. Akers, W. W., Kelley, R. E. and Lipscomb, T. G., 1954, Carbon dioxide-propane system, Ind. Eng. Chem., Vol. 46, pp.2535-2536 https://doi.org/10.1021/ie50540a039
  6. Hamam, S. E. M. and Lu, J. B. C. - Y, 1976, Isothermal vapour-liquid equilibria in binary system propane-carbon dioxide, Chem. Eng. Data, Vol. 21, pp.200-204 https://doi.org/10.1021/je60069a020
  7. Acosta, J. C., Hevia, E. and Leipziger, S., 1984, Dew and bubble point measurements for carbon dioxide-propane mixtures, J. Chem Eng. Data, Vol. 29, pp.304-309 https://doi.org/10.1021/je00037a024
  8. Niesen, V. G. and Rainwater, J. C., 1990, Critical locus, (vapour + liquid) equilibria, and coexisting densities of karbon dioxide + propane) at temperature from 311 K to 361 K, J. Chern. Thermodyn, Vol. 22, pp. 777-795 https://doi.org/10.1016/0021-9614(90)90070-7
  9. Chen, J. and Kruse, H., 1995, Calculating circulation concentration of zeotropic refrigerant mixtures, HVAC&R Research, Vol. 1, No.3, pp. 219-231 https://doi.org/10.1080/10789669.1995.10391320