Prediction of vapor–liquid equilibria for the Pb-X (X=Ag, Cu and Sn) systems in vacuum distillation using ab initio methods and Wilson equation

2016 ◽  
Vol 417 ◽  
pp. 25-28 ◽  
Author(s):  
XiaoMei Yang ◽  
XiuMin Chen ◽  
Cheng Zhang ◽  
XiaoGuang Xie ◽  
Bin Yang ◽  
...  
2017 ◽  
Vol 46 (7) ◽  
pp. 1514-1521 ◽  
Author(s):  
Xiumin Chen ◽  
Baoqiang Xu ◽  
Bin Yang ◽  
Dachun Liu ◽  
HongWei Yang

2015 ◽  
Vol 405 ◽  
pp. 68-72 ◽  
Author(s):  
Cheng Zhang ◽  
WenLong Jiang ◽  
Bin Yang ◽  
DaChun Liu ◽  
BaoQiang Xu ◽  
...  

2012 ◽  
Vol 38 (2) ◽  
pp. 76-79 ◽  
Author(s):  
Shigetoshi Kobuchi ◽  
Kenji Ishige ◽  
Kei Takakura ◽  
Setsuko Yonezawa ◽  
Kenji Fukuchi ◽  
...  

Author(s):  
Junjie Xu ◽  
Jingbao Gao ◽  
Lingxin Kong ◽  
Baoqiang Xu ◽  
Bin Yang ◽  
...  

In this study, experimental vapor-liquid equilibria data of the ternary Pb-Sn-Sb alloy system are determined using a new experimental method. The experimental VLE data passed the thermodynamic consistency test(Van Ness test), suggesting that the experimental results are reliable. The activities of the components of Pb-Sn-Sb ternary alloy and those of the corresponding three constituent binaries were calculated using the Wilson equation. The predicted values are in good agreement with the data determined from experiments, and the average relative deviation and average standard deviation were smaller than ? 4.00%and ? 0.03for all constituent binaries, respectively, which indicates that the Wilson equation is reliable for calculating the activity of the components of the Pb-Sn-Sb ternary alloy. The VLE data of the Pb-Sn and Sb-Sn binary alloys and Pb-Sn-Sb ternary alloy were calculated based on the VLE theory and Wilson equation. The calculated VLE data were in good agreement with the data determined from experiments, indicating that this method is reliable for calculating the VLE of alloy systems. The proposed study offers a valid method for analyzing the composition of products that are dependent on the distillation temperature and system pressure during vacuum distillation, which is of great significance to the experimental design of this process.


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