| Description |
1 online resource : illustrations |
| Contents |
Preface; Contents; Recommendation for Further Reading: Literature; 1 Planning of Distillation and Absorption Columns; 1.1 Planning Information; 1.2 Mass Balance for the Separation Task; 1.3 Separation Conditions; 1.4 Vapour-Liquid Equilibrium [4]; 1.4.1 The Ideal Equilibrium According to Raoult-Dalton; 1.4.2 Equations of State; 1.4.3 Equilibrium Models for Non-polar Materials Considering the Non-ideal Behaviour in the Liquid Phase Based on Pure Component Data |
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1.4.4 Equilibrium Models for Polar Components with High Non-ideal Behaviour in the Liquid Phase1.5 Energy and Mass Balance in the Column; 1.5.1 Mass Balance (Fig. 1.4); 1.5.2 Energy Balance (Fig. 1.5); 1.5.3 Required Column Diameter; 1.6 Selection of Column Internals; 1.7 Condensers [2]; 1.8 Reboiler [2]; 1.9 Vacuum Pumps [3]; 1.10 Control Facilities [5]; 1.11 Heating Systems with Steam or Hot Oil [3]; 1.11.1 Heat Transfer Coefficients; 1.11.2 Steam Heating [3]; 1.11.3 Heating with Hot Oil [3]; 1.12 Cooling Systems [3] |
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1.12.1 Cooling Water Circulation Systems1.12.2 Comparison Between a Cooling Tower and an Air Cooler; 1.12.3 Cooling Water by Evaporating a Refrigerant or Adiabatic Evaporation; 1.12.4 Direct Condensation in Columns [6]; References; 2 Equilibria, Bubble Points, Dewpoints, Flash Calculations, and Activity Coefficients; 2.1 Vapour Pressure Calculations; 2.2 Phase Equilibrium of Ideal Binary Mixtures; 2.3 Bubble Point Calculation; 2.4 Dew Point Calculation; 2.5 Dew Point Calculation of Vapour Containing Inert Gases |
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2.6 Dew and Bubble Point Lines of Ideal Binary Mixtures2.7 The Bubble Point and Dew Point of Immiscible Mixtures; 2.8 Flash Calculations for Ideal Binary Mixtures [1]; 2.9 Calculation of the Equilibrium and the Bubble and Dew Point Temperatures of Ideal Multi-component Mixtures; 2.10 Flash Calculations for Ideal Multi-component Mixtures [2]; 2.11 Phase Equilibrium of Non-ideal Binary Mixtures; 2.12 Calculation of the Activity Coefficients; 2.12.1 Calculation According to Wilson for Miscible Components [8] |
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2.12.2 Calculation According to NRTL for Partially Miscible Components with Two Liquid Phases [9]2.12.3 Calculation According to Uniquac for Components with a Miscibility Gap; 2.12.4 Critical Comparison of the Activity Coefficients Calculated Using Different Models; 2.13 Bubble Point, Dew Point, and Flash Separation for Non-ideal Binary Mixtures; 2.14 Non-ideal Multi-component Mixtures; References; 3 Fractionation of Binary Mixtures; 3.1 Material Balance; 3.2 Vapoura-Liquid Equilibria; 3.2.1 Equilibria of Ideal Mixtures |
| Summary |
This book highlights the aspects that need to be considered when designing distillation columns in practice. It discusses the influencing parameters as well as the equations governing them, and presents several numerical examples. The book is intended both for experienced designers and for those who are new to the subject |
| Bibliography |
Includes bibliographical references |
| Notes |
Online resource; title from PDF title page (EBSCO, viewed November 03, 2017) |
| Subject |
Distillation apparatus -- Design and construction
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Distillation -- Design and construction
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SCIENCE -- Chemistry -- Industrial & Technical.
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TECHNOLOGY & ENGINEERING -- Chemical & Biochemical.
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Distillation apparatus -- Design and construction
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| Form |
Electronic book
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| Author |
Gbadamosi, R., author
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| ISBN |
9783319516882 |
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3319516884 |
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