Vapor–Liquid Equilibrium for Binary Mixtures of 3-Cyano-1-butene + RS-4-Vinyl-1-cyclohexene, 3-Cyano-1-butene + ZE-1-Cyano-2-butene and RS-4-Vinyl-1-cyclohexene + ZE-1-Cyano-2-butene

2018 ◽  
Author(s):  
Dao-Cai Wang ◽  
Chun-Long Wang ◽  
Ying-Jie Luo ◽  
Hang Song ◽  
Xiao-Peng Liu
Keyword(s):  
Binary Mixtures ◽  
Liquid Equilibrium ◽  
Vapor Liquid Equilibrium ◽  
Vapor Liquid

Vapor–Liquid Equilibrium Data for 1-Methyl-2-Pyrrolidone + (1-Butanol or 1-Hexene or Water) Binary Mixtures

2014 ◽  
Vol 59 (5) ◽  
pp. 1643-1650 ◽  
Author(s):  
Ranjeetha Hirawan ◽  
Sumit Sinha ◽  
Samuel A. Iwarere ◽  
J. David Raal ◽  
Paramespri Naidoo ◽  
...  
Keyword(s):  
Binary Mixtures ◽  
Liquid Equilibrium ◽  
Vapor Liquid Equilibrium ◽  
Equilibrium Data ◽  
Vapor Liquid

Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor−Liquid Equilibrium at 101.3 kPa for Binary Mixtures of Methanol + Ethyl Lactate and 1-Propanol + Ethyl Lactate

2010 ◽  
Vol 55 (7) ◽  
pp. 2652-2652 ◽  
Author(s):  
José M. Resa ◽  
Emilio A. Cepeda ◽  
José M. Goenaga ◽  
Álvaro Ramos ◽  
Sofía Aguirre ◽  
...  
Keyword(s):  
Refractive Index ◽  
Binary Mixtures ◽  
Speed Of Sound ◽  
Ethyl Lactate ◽  
Liquid Equilibrium ◽  
Vapor Liquid Equilibrium ◽  
Vapor Liquid

Vapor–liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes

2007 ◽  
Vol 262 (1-2) ◽  
pp. 32-36 ◽  
Author(s):  
M. Radhamma ◽  
P. Venkatesu ◽  
T. Hofman ◽  
M.V. Prabhakara Rao
Keyword(s):  
Binary Mixtures ◽  
Liquid Equilibrium ◽  
Substituted Benzenes ◽  
Vapor Liquid Equilibrium ◽  
Vapor Liquid

A Neuro-fuzzy Model as a Predictive Tool for the Vapor-liquid Equilibrium of Binary Mixtures

2013 ◽  
Vol 31 (1) ◽  
pp. 68-79 ◽  
Author(s):  
S. M. Hosseini-Nasab ◽  
M. Manteghian ◽  
M. V. Sefti ◽  
A. A. Izadpanah ◽  
M. Zare
Keyword(s):  
Binary Mixtures ◽  
Fuzzy Model ◽  
Liquid Equilibrium ◽  
Predictive Tool ◽  
Vapor Liquid Equilibrium ◽  
Neuro Fuzzy ◽  
Vapor Liquid

Vapor–Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa

2013 ◽  
Vol 58 (11) ◽  
pp. 3054-3060 ◽  
Author(s):  
Zhigang Zhang ◽  
Peng Jia ◽  
Donghao Huang ◽  
Ming Lv ◽  
Yan Du ◽  
...  
Keyword(s):  
Binary Mixtures ◽  
Liquid Equilibrium ◽  
Vapor Liquid Equilibrium ◽  
Vapor Liquid

Molecular models for the vapor-liquid equilibrium of simple binary mixtures

2001 ◽  
Vol 22 (5) ◽  
pp. 531-538
Author(s):  
C. A. Faúndez ◽  
A. Mulero ◽  
F. Cuadros
Keyword(s):  
Binary Mixtures ◽  
Molecular Models ◽  
Liquid Equilibrium ◽  
Vapor Liquid Equilibrium ◽  
Vapor Liquid

Isothermal Vapor-Liquid Equilibrium Measurement of Isobutanol + Isooctane/N-Heptane Binary Mixtures at Temperatures Range of 303.15-323.15 K

2020 ◽  
Vol 840 ◽  
pp. 501-506
Author(s):  
Ardika Nurmawati ◽  
Rizky Tetrisyanda ◽  
Gede Wibawa
Keyword(s):  
Vapor Pressure ◽  
Binary Mixtures ◽  
Published Data ◽  
Positive Deviation ◽  
Average Absolute Deviation ◽  
Liquid Equilibrium ◽  
Absolute Deviation ◽  
Vapor Liquid Equilibrium ◽  
Mole Fraction Range ◽  
Vapor Liquid

The addition of alcohol as an oxygenated compound in gasoline blends may increase the vapor pressure of gasoline mixture. As a result, the study of vapor-liquid equilibrium for gasoline component and alcohol is necessary. In this study, the vapor-liquid equilibrium of isobutanol – isooctane/n-heptane blends were obtained experimentally at temperatures in the range 303.15 to 323.15 K using modified simple quasi-static ebulliometer. The apparatus was validated by comparing the vapor pressure of pure isobutanol, isooctane, and n-heptane with the published data and giving average absolute deviation (AAD) between experimental and calculated ones with magnitude less than 1.0%. The addition of isobutanol with the mole fraction range from 0.2 to 0.6 would increase the vapor pressure of the isooctane and n-heptane up to 12% and 14% respectively. The vapor pressure of binary mixtures was correlated with the Wilson, Non-random two-liquid (NRTL), and Universal quasi-chemical (UNIQUAC) equations with AAD 1.6%, 1.5%, and 1.7%, respectively for isobutanol + isooctane system and 1.8%, 1.7%, and 2.0%, respectively for isobutanol + n-heptane system. The systems studied show positive deviation from Raoult’s Law.

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