Vapour–liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a)+dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3MPa-Reference-Cited by-同舟云学术

Vapour–liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a)+dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3MPa

Published:2005-03 Issue:1-2 Volume:230 Page:184-191
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Valtz Alain,Gicquel Leila,Coquelet Christophe,Richon Dominique

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference21 articles.

1. Vapor–liquid equilibrium data for the propane+1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 293.16 to 353.18 K and pressures up to 3.4 MPa

2. Vapor–liquid equilibrium data for the CO2 + 1,1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa

3. Vapor−Liquid Equilibrium Data for the Azeotropic Difluoromethane + Propane System at Temperatures from 294.83 to 343.26 K and Pressures up to 5.4 MPa

4. Vapour–liquid equilibrium data for the difluoromethane+1,1,1,2,3,3,3-heptafluoropropane system at temperatures from 283.20 to 343.38 K and pressures up to 4.5 MPa

5. Vapor–liquid equilibrium data for the carbon dioxide (CO2) + difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa

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