Modified Vapor Pressure Model Based on Corresponding-States Principle for Pure and Mixed Refrigerants
Author:
Affiliation:
1. Insitute of Building Energy & Sustainability Technology, School of Human Settlement and Civil Engineering, Xi’an Jiaotong University
2. Key Laboratory of Thermo-Fluid Science and Engineering, Ministry of Education, Xi’an Jiaotong University
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
https://www.jstage.jst.go.jp/article/jcej/50/11/50_17we024/_pdf
Reference55 articles.
1. Benning, A. F. and R. C. McHarness; “Thermodynamic Properties of Fluorochloromethanes and -Ethanes Vapor Pressure of Three Fluorochloromethanes and Trifluorotichloroethane,” Ind. Eng. Chem., 32, 497–499 (1940)
2. Bobbo, S., R. Stryjek, N. Elvassore and A. Bertucco; “A Recirculation Apparatus for Vapor–Liquid Equilibrium Measurements of Refrigerants Binary Mixtures of R600a, R134a and R236fa,” Fluid Phase Equilib., 150–151, 343–352 (1998)
3. Bobbo, S., R. Camporese and R. Stryjek; “Vapor–Liquid Equilibria for Difluoromethane (R32) + and Pentafluoroethane (R125) + 1,1,1,3,3,3-Hexafluoropropane (R236fa) at 303.2 and 323.3 K,” J. Chem. Eng. Data, 44, 349–352 (1999)
4. Bobbo, S., L. Fedele, M. Scattolini and R. Camporese; “Isothermal VLE Measurements for the Binary Mixtures HFC-134a+HFC-245fa and HC-600a+HFC-245fa,” Fluid Phase Equilib., 185, 255–264 (2001)
5. Brown, J. S., G. Di Nicola, L. Fedele, S. Bobbo and C. Zilio; “Saturated Pressure Measurements of 3,3,3-Trifluoroprop-1-ene (R1243zf) for Reduced Temperatures Ranging from 0.62 to 0.98,” Fluid Phase Equilib., 351, 48–52 (2013)
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