Author: Howard L. Wilson
Publisher:
ISBN:
Category : Hydrogen fluoride
Languages : en
Pages : 0
Book Description
Modeling Vapor-liquid Equilibrium Data for Systems Containing Hydrogen Fluoride
Author: Howard L. Wilson
Publisher:
ISBN:
Category : Hydrogen fluoride
Languages : en
Pages : 0
Book Description
Publisher:
ISBN:
Category : Hydrogen fluoride
Languages : en
Pages : 0
Book Description
Modeling Vapor-liquid Equilbrium Data for Systems Containing Hydrogen Fluoride
Author: Howard L. Wilson
Publisher:
ISBN:
Category : Hydrogen fluoride
Languages : en
Pages : 229
Book Description
Publisher:
ISBN:
Category : Hydrogen fluoride
Languages : en
Pages : 229
Book Description
Low-temperature vapor-liquid equilibria in ternary and quaternary systems containing hydrogen, nitrogen, methane and ethane
Author: Harry Francis Cosway
Publisher:
ISBN:
Category : Science
Languages : en
Pages : 171
Book Description
Publisher:
ISBN:
Category : Science
Languages : en
Pages : 171
Book Description
VAPOR-LIQUID EQUILIBRIA OF LIGHT HYDROCARBON SYSTEMS CONTAINING HYDROGEN AT LOW TEMPERATURE.
Author: ALVIN LYNN BENHAM
Publisher:
ISBN:
Category : Hydrocarbons
Languages : en
Pages : 288
Book Description
Publisher:
ISBN:
Category : Hydrocarbons
Languages : en
Pages : 288
Book Description
Vapor-liquid Equilibrium Data Collection: Aqueous-organic systems
Author: Jürgen Gmehling
Publisher:
ISBN:
Category : Chemistry, Organic
Languages : en
Pages : 570
Book Description
Publisher:
ISBN:
Category : Chemistry, Organic
Languages : en
Pages : 570
Book Description
Vapor-liquid Equilibrium Data
Author: Shūzō Ōe
Publisher: Elsevier Science & Technology
ISBN:
Category : Science
Languages : en
Pages : 784
Book Description
Vapor-liquid equilibrium (VLE) data are necessary for the design and operation of distillation processes. It is absolutely impossible to determine a distillation process without VLE data. The author of this book has had much experience designing and constructing distillation processes and towers and knows that VLE data must be easily retrievable, readily comprehensible, and precise. This volume contains the most important VLE data for 1,446 binary systems with Wilson parameters determined by computer processing. The data are also presented graphically. The Wilson equation, which is known as one of the most applicable to multicomponent systems, is employed for computer-aided determination of the optimum parameters using the non-linear least squares method.
Publisher: Elsevier Science & Technology
ISBN:
Category : Science
Languages : en
Pages : 784
Book Description
Vapor-liquid equilibrium (VLE) data are necessary for the design and operation of distillation processes. It is absolutely impossible to determine a distillation process without VLE data. The author of this book has had much experience designing and constructing distillation processes and towers and knows that VLE data must be easily retrievable, readily comprehensible, and precise. This volume contains the most important VLE data for 1,446 binary systems with Wilson parameters determined by computer processing. The data are also presented graphically. The Wilson equation, which is known as one of the most applicable to multicomponent systems, is employed for computer-aided determination of the optimum parameters using the non-linear least squares method.
Low-temperature Vapor-liquid Equilibria in Ternary and Quaternary Systems Containing Hydrogen, Nitrogen, Methane and Ethane
Author: Harry F. Cosway
Publisher:
ISBN:
Category : Chemical equilibrium
Languages : en
Pages : 167
Book Description
Publisher:
ISBN:
Category : Chemical equilibrium
Languages : en
Pages : 167
Book Description
Vapor-liquid Equilibrium Data Collection
Author: Jürgen Gmehling
Publisher:
ISBN:
Category : Liquids
Languages : en
Pages : 640
Book Description
Publisher:
ISBN:
Category : Liquids
Languages : en
Pages : 640
Book Description
Vapor-liquid Equilibrium Data Collection
Author: J. Gmehling
Publisher:
ISBN:
Category : Science
Languages : en
Pages : 608
Book Description
Publisher:
ISBN:
Category : Science
Languages : en
Pages : 608
Book Description
Vapor-Liquid Equilibria Using Unifac
Author: Aage Fredenslund
Publisher: Elsevier
ISBN: 0444601503
Category : Technology & Engineering
Languages : en
Pages : 393
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.
Publisher: Elsevier
ISBN: 0444601503
Category : Technology & Engineering
Languages : en
Pages : 393
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.