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Distillation and Rectification (Hardcover)
Loot Price: R3,700
Discovery Miles 37 000
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Distillation and Rectification (Hardcover)
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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 -
General
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