Distillation and Rectification

Emil Kirschbaum

ISBN 10: 0820600180 / ISBN 13: 9780820600185

Published by Chemical Publishing Company, 1948

About this Item

nach der Bestellung gedruckt Neuware - Printed after ordering - A. FundamentalsB. TheoryI. UnitsII. Interrelation between vapor concentration and partial pressure of vapor in multicomponent mixturesIII. Equilibrium of boiling multicomponent mixturesIV. Partial condensation of mixturesV. Heat of evaporation of mixturesC. Separation of liquids by simple distillation; the simple pot stillI. Data for computationII. Design of kettle stillsIII. Separation by distillation and partial condensationD. The rectifying columnI. Effect of rectifying platesII. Hookup of reflux condensersIII. Layout of a batch-type distillation unitIV. Computation of the number of plates for a batch type distillation unitV. Minimum reflux ratio and actual reflux ratio for batch-type rectifiersVI. The rectification mechanism on interchanger platesVII. Heat consumption and reboil heat for a pot still and rectifying columnE. Continuous distilling equipment having rectifying and stripping sectionsI. Determination of the number of platesII. Minimum reflux ratio of a continuous rectifying unit for separating binary mixturesIII. The actual reflux ratio of a continuous rectifying unitIV. Mass-concentration interrelationsV. Heat requirementsVI. Reduction of heat requirementsVII. Layout of continuous rectifying equipment for handling binary mixturesVII I. Special casesIX. Location of the feed pointX. Heat lossesXI. Variation of the molar heat of evaporation in the interchanger columnF. Treatment of rectification using enthalpy-concentration diagramsI. The rectifying columnII. The continuous rectifying unitG. Separating mixtures containing more than two componentsI. Eliminating small amounts of certain components in a mixtureII. Separation of ideal ternary mixturesIII. Number of rectifying columns required to separate multicomponent mixtures and their hookupIV. Rectifying ideal mixtures of more than three componentsH. Determining the dimensions of rectifying columns with interchanger plates; plate efficiencyI. Cap-type and tunnel-type platesII. Sieve platesIII. Comparison of cap-type and sieve-type platesIV. Influence of the direction of flow of the phases on the rectification effect of a plate; liquid mixing, vapor mixing, counterflow arid parallel flowV. Rectifying plate designJ. Rectification in packed columnsI. General remarksII. Determining the column height by means of the corresponding theoretical plate number; different types of packingsIII. Determination of column height from the heat transmission coefficient between phases; liquid distribution within the columnIV. Pressure loss in packed columnsK. DetailsI. Heat exchangersII. Control equipmentL. Molecular distillationM. AppendixI. Equilibrium data for binary mixturesII. Heats of evaporation of various materials at ¿ 760 mm HgIII. Specific heats and specific weights of liquidsIV. Molecular weightsV. Conversion tablesN. Review by the translator of progress made since the original publicationIndex.

Seller Inventory # 9780820600185

Bibliographic Details

• Title: Distillation and Rectification
• Publisher: Chemical Publishing Company
• Publication Date: 1948
• Language: English
• ISBN 10: 0820600180
• ISBN 13: 9780820600185
• Binding: Buch
• Condition: Neu
• Dimensions: 235W x 157H x 31D millimeters 235 millimeters width by 157 millimeters height by 31 millimeters depth
• Weight: 867 grams

About this title

Synopsis

A. Fundamentals - B. Theory - I. Units - II. Interrelation between vapor concentration and partial pressure of vapor in multicomponent mixtures - III. Equilibrium of boiling multicomponent mixtures - IV. Partial condensation of mixtures - V. Heat of evaporation of mixtures - C. Separation of liquids by simple distillation; the simple pot still - I. Data for computation - II. Design of kettle stills - III. Separation by distillation and partial condensation - D. The rectifying column - I. Effect of rectifying plates - II. Hookup of reflux condensers - III. Layout of a batch-type distillation unit - IV. Computation of the number of plates for a batch type distillation unit - V. Minimum reflux ratio and actual reflux ratio for batch-type rectifiers - VI. The rectification mechanism on interchanger plates - VII. Heat consumption and reboil heat for a pot still and rectifying column - E. Continuous distilling equipment having rectifying and stripping sections - I. Determination of the number of plates - II. Minimum reflux ratio of a continuous rectifying unit for separating binary mixtures - III. The actual reflux ratio of a continuous rectifying unit - IV. Mass-concentration interrelations - V. Heat requirements - VI. Reduction of heat requirements - VII. Layout of continuous rectifying equipment for handling binary mixtures - VII I. Special cases - IX. Location of the feed point - X. Heat losses - XI. Variation of the molar heat of evaporation in the interchanger column - F. Treatment of rectification using enthalpy-concentration diagrams - I. The rectifying column - II. The continuous rectifying unit - G. Separating mixtures containing more than two components - I. Eliminating small amounts of certain components in a mixture - II. Separation of ideal ternary mixtures - III. Number of rectifying columns required to separate multicomponent mixtures and their hookup - IV. Rectifying ideal mixtures of more than three components - H. Determining the dimensions of rectifying columns with interchanger plates; plate efficiency - I. Cap-type and tunnel-type plates - II. Sieve plates - III. Comparison of cap-type and sieve-type plates - IV. Influence of the direction of flow of the phases on the rectification effect of a plate; liquid mixing, vapor mixing, counterflow arid parallel flow - V. Rectifying plate design - J. Rectification in packed columns - I. General remarks - II. Determining the column height by means of the corresponding theoretical plate number; different types of packings - III. Determination of column height from the heat transmission coefficient between phases; liquid distribution within the column - IV. Pressure loss in packed columns - K. Details - I. Heat exchangers - II. Control equipment - L. Molecular distillation - M. Appendix - I. Equilibrium data for binary mixtures - II. Heats of evaporation of various materials at - 760 mm Hg - III. Specific heats and specific weights of liquids - IV. Molecular weights - V. Conversion tables - N. Review by the translator of progress made since the original publication - Index -