Vapor-liquid equilibria for pentafluoroethane plus propane and difluoromethane plus propane systems over a temperature range from 253.15 to 323.15 K
- Authors
- Kim, JH; Kim, MS; Kim, Y
- Issue Date
- 2003-09-01
- Publisher
- ELSEVIER
- Citation
- FLUID PHASE EQUILIBRIA, v.211, no.2, pp.273 - 287
- Abstract
- This paper provides vapor-liquid equilibrium (VLE) data obtained for two binary systems of pentafluoroethane (R125) + propane (R290) and difluoromethane (R32) + R290 over a temperature range from 253.15 to 323.15 K. The measurement of VLE was performed at isothermal conditions in a vapor recirculation apparatus. Both systems form azeotropes in the temperature range of this study. The experimental results were well correlated with the Peng-Robinson equation of state (PR EoS) using one parameter van der Waals one fluid model. The binary interaction parameters were optimized using the experimental data of bubble point pressure. A comparison with published experimental VLE data has been carried out by means of the PR equation of state. (C) 2003 Elsevier B.V. All rights reserved.
- Keywords
- vapor-liquid equilibria; azeotrope; Peng-Robinson EoS; pentafluoroethane; difluoromethane; propane
- ISSN
- 0378-3812
- URI
- https://pubs.kist.re.kr/handle/201004/138244
- DOI
- 10.1016/S0378-3812(03)00237-1
- Appears in Collections:
- KIST Article > 2003
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