Vapor-liquid Equilibria and Group Contribution Theories for Binary Systems of Alcohols by Hydrocarbons PDF Download
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Author: Shuen-Cheng Hwang
Publisher:
ISBN:
Category :
Languages : en
Pages : 484
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Book Description
Author: Shuen-Cheng Hwang
Publisher:
ISBN:
Category :
Languages : en
Pages : 484
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Book Description
Author: Andrzej Mączyński
Publisher:
ISBN:
Category : Alcohols
Languages : en
Pages : 274
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Book Description
Author:
Publisher:
ISBN:
Category : Hydrocarbons
Languages : en
Pages : 0
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Book Description
Author: Andrzej Mączyński
Publisher:
ISBN:
Category : Alcohols
Languages : en
Pages : 270
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Book Description
Author:
Publisher:
ISBN:
Category : Alcohols
Languages : en
Pages :
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Book Description
Author: Andrzej Mączyński
Publisher:
ISBN:
Category : Hydrocarbons
Languages : en
Pages : 234
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Book Description
Author: Andrzej Mączyński
Publisher:
ISBN:
Category : Alcohols
Languages : en
Pages : 260
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Book Description
Author:
Publisher:
ISBN: 9788387576318
Category : Alcohols
Languages : en
Pages :
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Book Description
Author: Andrzej Mączyński
Publisher:
ISBN:
Category : Hydrocarbons
Languages : en
Pages : 282
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Book Description
Author: Aage Fredenslund
Publisher: Elsevier
ISBN: 0444601503
Category : Technology & Engineering
Languages : en
Pages : 393
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Book Description
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.
