Vapor-liquid equilibrium data concerning refrigerant systems Example (R116+R143a)

被引：7

作者：

Madani, Hakim ^{[1
]}

Coquelet, Christophe ^{[2
]}

Richon, Dominique ^{[2
]}

机构：

[1] Univ Batna, Lab Etud Syst Energet Ind, Batna, Algeria

[2] CNRS FRE 2861, CEP TEP, ParisTech, Mines Paris, F-77305 Fontainebleau, France

来源：

TERRAGREEN 2012: CLEAN ENERGY SOLUTIONS FOR SUSTAINABLE ENVIRONMENT (CESSE) | 2012年 / 18卷

关键词：

VLE data; refrigerants; R-116; R-143a; Supercritical gas solubility; Critical points; Phase diagrams; EQUATION-OF-STATE; PHASE-EQUILIBRIA; CRITICAL-POINTS; TEMPERATURES; PRESSURES; MPA; MIXTURES; HEXAFLUOROETHANE;

D O I：

10.1016/j.egypro.2012.05.014

中图分类号：

TE [石油、天然气工业]; TK [能源与动力工程];

学科分类号：

0807 ; 0820 ;

摘要：

Development of modern refrigeration systems is critical for the success of new global environmental protection efforts. The binary system of refrigerants: Hexafluoroethene (R116) + 1,1,1-trifluoroethane (R143a), has been studied with the aim of providing PTxy data. Isothermal vapor-liquid equilibrium data have generated using the "static analytic" method from 258 to 328 K at pressures from 0.39 to 3.89 MPa. The model composed of the Peng-Robinson of state, the Mathias-Copeman alpha function, the Wong-Sandler mixing rules and the NRTL cell theory is applied herein to correlate the data and calculate the critical line.

引用

页码：21 / 34

页数：14

共 50 条

[41] Vapor-liquid equilibrium measurement for carbon dioxide (CO2)+ propylene (R1270) binary mixture at temperatures from subcritical to supercritical
Wu, Zirui
Sun, Rui
Shi, Lingfeng
Hu, Peng
Tian, Hua
Wang, Xuan
Shu, Gequn
INTERNATIONAL JOURNAL OF REFRIGERATION, 2024, 158 : 164 - 172
[42] Vapor-liquid equilibrium and diffusion coefficients of R32+[HMIM][FEP], R152a+[HMIM][FEP] and R161+[HMIM][FEP]
Liu, Xiangyang
Pan, Pei
He, Maogang
JOURNAL OF MOLECULAR LIQUIDS, 2018, 253 : 28 - 35
[43] Structural effect on the vapor-liquid equilibrium of toluene-ionic liquid systems
Yu, Gangqiang
Jiang, Yifan
Cheng, Jun
Lei, Zhigang
CHEMICAL ENGINEERING SCIENCE, 2019, 198 : 1 - 15
[44] Vapor-liquid equilibrium data for the binary mixture difluoroethane (HFC-32)+pentafluoroethane (HFC-125) of an alternative refrigerant
Han, Xiaohong
Chen, Guangming
Cui, Xiaolong
Wang, Qin
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2007, 52 (06) : 2112 - 2116
[45] Vapor-Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Horstmann, Sven
Constantinescu, Dana
Gmehling, Juergen
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2017, 62 (09) : 2776 - 2786
[46] Experimental measurements and correlation of vapor-liquid equilibrium and critical data for the CO2 + R1234yf and CO2 + R1234ze(E) binary mixtures
Juntarachat, Niramol
Valtz, Alain
Coquelet, Christophe
Privat, Romain
Jaubert, Jean-Noel
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2014, 47 : 141 - 152
[47] Vapor-liquid equilibrium for the ternary carbon dioxide-ethanol-nonane and decane systems
Arenas-Quevedo, Miguel G.
Galicia-Luna, Luis A.
Elizalde-Solis, Octavio
Perez-Pimienta, Jose A.
FLUID PHASE EQUILIBRIA, 2013, 338 : 30 - 36
[48] Application of molecular modeling to the vapor-liquid equilibrium of alkyl esters (biodiesel) and alcohols systems
Corazza, Marcos L.
Fouad, Wael A.
Chapman, Walter G.
FUEL, 2015, 161 : 34 - 42
[49] Isothermal vapor-liquid equilibrium data for the ethylene+1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
Subramoney, Shalendra Clinton
Courtial, Xavier
Naidoo, Paramespri
Coquelet, Christophe
Richon, Dominique
Ramjugernath, Deresh
FLUID PHASE EQUILIBRIA, 2013, 353 : 7 - 14
[50] Statistical regression of binary vapor-liquid equilibrium data for ternary phase equilibrium predictions
Zhang, NW
Zhang, Q
Zheng, XY
FLUID PHASE EQUILIBRIA, 1998, 147 (1-2) : 123 - 143

← 1 2 3 4 5 →