Distillation Rectification by Kirschbaum Emil (15 results)
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More imagesPublished by Chemical Publishing Company, 1948
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Published by Chemical Publishing Company, Incorporated, 1948
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Condition: New. Dieser Artikel ist ein Print on Demand Artikel und wird nach Ihrer Bestellung fuer Sie gedruckt. KlappentextA. 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. Pa…rtial cond.
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Published by Chemical Publishing Company, Incorporated, 1948
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Published by Chemical Publishing Company, Incorporated, 1948
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Buch. Condition: Neu. Distillation and Rectification | Emil Kirschbaum | Buch | Gebunden | Englisch | Chemical Publishing Company | EAN 9780820600185 | Verantwortliche Person für die EU: Libri GmbH, Europaallee 1, 36244 Bad Hersfeld, gpsr[at]libri[dot]de | Anbieter: preigu Print on Demand.
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Buch. Condition: Neu. 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.
