Experimental investigation on vapor liquid equilibrium and azeotropic behavior for the 1,1,1,2-tetrafluoroethane (R134a) + propane (R290) system at temperatures from 253.15 to 303.15 K

Author:

Qin Yanbin,Li Nanxi,Zhang Hua,Liu Baolin,Wu Chunfei,Wang ZilongORCID

Publisher

Elsevier BV

Subject

Mechanical Engineering,Building and Construction

Reference71 articles.

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2. Vapor–liquid equilibrium measurements and correlations for the binary mixture of difluoromethane+isobutane and the ternary mixture of propane+isobutane+difluoromethane. Fluid Phase Equilibria;Akasaka;Properties and Phase Equilibria for Product and Process Design,2007

3. Handbook-Fundamentals,2013

4. ASPEN Plus, (2020). Aspen Technology Inc., 200 Wheeler Road Burlington, MA, USA.

5. Vapor−Liquid Equilibrium Measurements and Correlation of the Binary Refrigerant Mixture Propane (HC-290) + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) at 278.15, 293.15, and 308.15 K;Bobbo;J. Chem. Eng. Data,2002

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