The Vapor-liquid Equilibrium of the System Methanol-ethanol-acetone and Its Component Binaries PDF Download
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Author: Hassanein Hamed Amer
Publisher:
ISBN:
Category :
Languages : en
Pages : 312
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Author: Hassanein Hamed Amer
Publisher:
ISBN:
Category :
Languages : en
Pages : 312
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Author: Soon Yuck Wong
Publisher:
ISBN:
Category : Chemical equilibrium
Languages : en
Pages : 0
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"In the field of synthetic liquid fuels and organic chemicals there is considerable industrial interest in Fischer-Tropsch-type processes for the production of liquid hydrocarbons and various organic chemicals as by-products. Processes developed primarily for the production of oxygenated organic chemicals by partial oxidation of paraffin hydrocarbons are also in commercial operation. For both processes, recovery and purification of the product constituents by fractional distillation constitute a major problem. Of primary importance to solutions of the problem are the availability of reliable vapor-liquid equilibrium data on the various systems encountered. The need for suitable data is increased by the fact that practically all existing vapor-liquid equilibrium data are for atmospheric pressure only, whereas actual distillation operations are most frequently conducted at pressure above one atmosphere because of favorable economics, design, operations, and control requirements. It is obvious that reliable data at pressure other than one atmosphere and in particular, superatmospheric data are needed. More fundamentally important however, is the need for complete and extended data to evaluate and test the applicability of proposed correlations of the vapor-liquid data. Such extension and correlation involve the change of vapor-liquid equilibria with temperature or pressure, the determination of these data with a minimum of experimental effort, and the extension of binary data into reliable ternary data. Of the numerous oxygenated components produced by the aforementioned processes, acetone, methanol, and water constitute the major portion of the crude products. Binary and ternary systems containing these components have been evaluated and the results reported herein"--Leaves iii-iv
Author: Richard A. Wilsak
Publisher:
ISBN:
Category :
Languages : en
Pages :
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Author: James Michael Willock
Publisher:
ISBN:
Category : Vapor-liquid equilibrium
Languages : en
Pages : 210
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Author: Scott W. Campbell
Publisher:
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Category :
Languages : en
Pages :
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Author: Huei Luo
Publisher:
ISBN:
Category : Vapor-liquid equilibrium
Languages : en
Pages : 404
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Author: Aage Fredenslund
Publisher: Elsevier
ISBN: 0444601503
Category : Technology & Engineering
Languages : en
Pages : 393
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Vapor-Liquid Equilibria Using UNIFAC: A Group-Contribution Method focuses on the UNIFAC group-contribution method used in predicting quantitative information on the phase equilibria during separation by estimating activity coefficients. Drawing on tested vapor-liquid equilibrium data on which UNIFAC is based, it demonstrates through examples how the method may be used in practical engineering design calculations. Divided into nine chapters, this volume begins with a discussion of vapor and liquid phase nonidealities and how they are calculated in terms of fugacity and activity coefficients, respectively. It then introduces the reader to the UNIFAC method and how it works, the procedure used in establishing the parameters needed for the model, prediction of binary and multicomponent vapor-liquid equilibria for a large number of systems, the potential of UNIFAC for predicting liquid-liquid equilibria, and how UNIFAC can be used to solve practical distillation design problems. This book will benefit process design engineers who want to reliably predict phase equilibria for designing distillation columns and other separation processes.
Author: Leon Robert Kiley
Publisher:
ISBN:
Category :
Languages : en
Pages : 534
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Author: Antonio Oswaldo Lau
Publisher:
ISBN:
Category :
Languages : en
Pages : 256
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Author: Chester Bryan Buford
Publisher:
ISBN:
Category : Equilibrium
Languages : en
Pages : 84
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