Author:
Han Xiao-hong,Chen Guang-ming,Wang Qin,Cui Xiao-long
Publisher
Zhejiang University Press
Reference19 articles.
1. Bobbo, S., Roman, S., Nicola, E., Alberto, B., 1998. A recirculation apparatus for vapor-liquid equilibrium measurements of refrigerants. Binary mixtures of R600a, R134a, R236fa.Fluid Phase Equilibria,150–151: 343–352.
2. Boulouvalas, C., Spiliotis, N., Coutsikos, P., Tzouvaras, N., 1994. Prediction of vapor-liquid equilibrium with LCVM model: A linear combination of the Huron-Vidal and Michelsen mixing rules coupled with the original UNIFAC and the t-mPR equation of state.Fluid Phase Equilibria,92: 75–106.
3. Coquelet, C., Hong, D. N., Chareton, A., Baba-Ahmed, A., Richon, D., 2003. Vapor-liquid equilibrium data for the difluoromethane+1,1,1,2,3,3,3-heptafluoropropane system at temperatures from 283.2 to 343.38 K and pressures up to 4.5 MPa.Int. J. of Refr.,26: 559–565.
4. Han, X. H., Wang, Q., Chen, G. M., Cui, X. L., 2005. Extension of Huron-type mixing rule to three-parameter Harmens-Knapp cubic equation of state.Chemical Research in Chinese Universities,21(3): 209–212.
5. Holderbaum, T., Gmehling, J., 1991. PSRK: A group contribution equation of state based on UNFIAC.Fluid Phase Equilibria,70: 251–265.