Calculating the Liquid–Gas Equilibrium in the Fischer–Tropsch Synthesis.

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Title: Calculating the Liquid–Gas Equilibrium in the Fischer–Tropsch Synthesis.
Authors: Mikhailova, I. A.1, Fadeev, S. I.2, Khasin, A. A.1, Chermashentseva, G. K., Kirillov, V. A.
Source: Theoretical Foundations of Chemical Engineering. Mar/Apr2003, Vol. 37 Issue 2, p167-171. 5p.
Subjects: Equations of state, Coal gas, Liquids, Algorithms, Molecular weights, Chemical engineering
Abstract: The problem of determining the equilibrium composition of the gas phase from the known composition of the liquid phase is analyzed in terms of the Redlich-Kwong-Soave equation of state modified by Wang. An effective algorithm is suggested for solving this problem for systems with an arbitrary number of components. The molecular-weight distribution of the Fischer-Tropsch synthesis products can be estimated by calculating the composition of the gas phase from composition data for the liquid phase resulting from the reaction. [ABSTRACT FROM AUTHOR]
Copyright of Theoretical Foundations of Chemical Engineering is the property of Springer Nature and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract. (Copyright applies to all Abstracts.)
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  Data: The problem of determining the equilibrium composition of the gas phase from the known composition of the liquid phase is analyzed in terms of the Redlich-Kwong-Soave equation of state modified by Wang. An effective algorithm is suggested for solving this problem for systems with an arbitrary number of components. The molecular-weight distribution of the Fischer-Tropsch synthesis products can be estimated by calculating the composition of the gas phase from composition data for the liquid phase resulting from the reaction. [ABSTRACT FROM AUTHOR]
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  Data: <i>Copyright of Theoretical Foundations of Chemical Engineering is the property of Springer Nature and its content may not be copied or emailed to multiple sites without the copyright holder's express written permission. Additionally, content may not be used with any artificial intelligence tools or machine learning technologies. However, users may print, download, or email articles for individual use. This abstract may be abridged. No warranty is given about the accuracy of the copy. Users should refer to the original published version of the material for the full abstract.</i> (Copyright applies to all Abstracts.)
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