Distillation And Rectification,Used

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 batchtype distillation unit IV. Computation of the number of plates for a batch type distillation unit V. Minimum reflux ratio and actual reflux ratio for batchtype 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. Massconcentration 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 enthalpyconcentration 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. Captype and tunneltype plates II. Sieve plates III. Comparison of captype and sievetype 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