Effect to Reflux Ration on Separation of Azeotropic Mixtures in Batch Distillation Column

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ISBN 13 :
Total Pages : 39 pages
Book Rating : 4.:/5 (953 download)

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Book Synopsis Effect to Reflux Ration on Separation of Azeotropic Mixtures in Batch Distillation Column by : Wan Norazlinda Wan Zakaria

Download or read book Effect to Reflux Ration on Separation of Azeotropic Mixtures in Batch Distillation Column written by Wan Norazlinda Wan Zakaria and published by . This book was released on 2010 with total page 39 pages. Available in PDF, EPUB and Kindle. Book excerpt: The purpose of this study is to investigate the effect of different reflux ratio on separation of azeotropic mixtures. The azeotropic mixtures used were Ethanol/Water, MTBE/Methanol and IPA/Water. The experimental studied were conducted using Bubble Cap Distillation with 10 numbers of stages at 1 atm. The composition of feed mixtures used were 40:60 v/v. In terms of reflux ratios it was set at 1.1, 1.2, 1.3 and 1.4. The product was collected from each experiment and analyzed using refractometer to determine its concentration. The standard curve of binary mixtures of each mixtures were used for quantifying the composition in the collecting samples. From the results obtained, best reflux ratio for Ethanol/Water is 1.1 (95.8%), 1.2 for IPA/Water ( 57.64 mol%) and 1.2 for MTBE/Methanol (47.57%). The results obtained were compared with the vapour composition of binary mixtures for ordinary distillation process which are without reflux ratio. By comparing the result with the data of the vapor composition for ordinary distillation, the best reflux ratio was determined. These binary mixtures cannot be separated completely by ordinary distillation because of closed boiling point between each component which formed the azeotrope. When two mixtures were mixed, the intermolecular attraction forces in all liquid may cause the mixture to form certain inseparable composition (where vapour and liquid composition) at equilibrium are equal. Further separation can be achieved by controlling the reflux ratio of the distillation process to improve the separation efficiency. This study verified that reflux ratio influence the efficiency of the column.

Design and Control of Distillation Systems for Separating Azeotropes

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Publisher : John Wiley & Sons
ISBN 13 : 1118209834
Total Pages : 553 pages
Book Rating : 4.1/5 (182 download)

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Book Synopsis Design and Control of Distillation Systems for Separating Azeotropes by : William L. Luyben

Download or read book Design and Control of Distillation Systems for Separating Azeotropes written by William L. Luyben and published by John Wiley & Sons. This book was released on 2011-12-06 with total page 553 pages. Available in PDF, EPUB and Kindle. Book excerpt: Hands-on guidance for the design, control, and operation of azeotropic distillation systems Following this book's step-by-step guidance, readers learn to master tested and proven methods to overcome a major problem in chemical processing: the distillation and separation of azeotropes. Practical in focus, the book fully details the design, control, and operation of azeotropic distillation systems, using rigorous steady-state and dynamic simulation tools. Design and Control of Distillation Systems for Separating Azeotropes is divided into five parts: Fundamentals and tools Separations without adding other components Separations using light entrainer (heterogeneous azeotropic distillation) Separations using heavy entrainer (extractive distillation) Other ways for separating azeotropes The distillation methods presented cover a variety of important industrial chemical systems, including the processing of biofuels. For most of these chemical systems, the authors explain how to achieve economically optimum steady-state designs. Moreover, readers learn how to implement practical control structures that provide effective load rejection to manage disturbances in throughput and feed composition. Trade-offs between steady-state energy savings and dynamic controllability are discussed, helping readers design and implement the distillation system that best meets their particular needs. In addition, economic and dynamic comparisons between alternative methods are presented, including an example of azeotropic distillation versus extractive distillation for the isopropanol/water system. With its focus on practical solutions, Design and Control of Distillation Systems for Separating Azeotropes is ideal for engineers facing a broad range of azeotropic separation problems. Moreover, this book is recommended as a supplemental text for undergraduate and graduate engineering courses in design, control, mass transfer, and bio-processing.

Distillation And Absorption

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Publisher : CRC Press
ISBN 13 : 9781560322573
Total Pages : 568 pages
Book Rating : 4.3/5 (225 download)

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Book Synopsis Distillation And Absorption by : K E Porter

Download or read book Distillation And Absorption written by K E Porter and published by CRC Press. This book was released on 1992-12-29 with total page 568 pages. Available in PDF, EPUB and Kindle. Book excerpt: Contains the papers presented at a symposium which aimed to address and record changes in distillation and absorption and to discuss new directions. Topics covered include: column sequencing; equipment; batch distillation; azeotropic and extractive distillation; packed columns and more.

Distillation and Rectification

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ISBN 13 :
Total Pages : 452 pages
Book Rating : 4.3/5 (91 download)

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Book Synopsis Distillation and Rectification by : Emil Kirschbaum

Download or read book Distillation and Rectification written by Emil Kirschbaum and published by . This book was released on 1948 with total page 452 pages. Available in PDF, EPUB and Kindle. Book excerpt: 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 -

Scale Up Study of Salt Added Batch Distillation of Azeotropic Mixture

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ISBN 13 :
Total Pages : 53 pages
Book Rating : 4.:/5 (953 download)

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Book Synopsis Scale Up Study of Salt Added Batch Distillation of Azeotropic Mixture by : Kok Jie Liew

Download or read book Scale Up Study of Salt Added Batch Distillation of Azeotropic Mixture written by Kok Jie Liew and published by . This book was released on 2013 with total page 53 pages. Available in PDF, EPUB and Kindle. Book excerpt: Solvent recovery is often practised in chemical industry especially in glove and catheter manufacturing. However, azeotropic behaviour in mixture (isopropanol-water binary mixture) complicates the separation process. Conventional batch distillation is no longer effective in recovering the solvent. Moreover, the unrecovered solvent will end up as toxic waste and disposal of such toxic waste is jeopardising to the environment. Experimental works were carried out and scaling up study was performed in order to solve these problems. The research objectives are twofold: (a) to determine optimum salt concentration for distilling IPA-water azeotropic mixture by using salt added batch distillation to recover IPA for purity more than 90 mol%, and (b) to study scaling up of salt added batch distillation unit for IPA-water azeotropic mixture from a laboratory scale to pilot plant scale. Two stages of procedures, which are laboratory scale and pilot plant experiments, were carried out. The optimum salt concentration and the scaling up were studied. The optimum salt concentration needed to break the azeotropic point of IPA-water mixture is generally decreasing as z1 is higher. Salt solution was dissolved to the still before distillation using laboratory scale and no reflux ratio can be controlled due to simpler apparatus. Results showed that 2.5 mol% and 1.57 mol% of calcium chloride salt has successfully recover 91 mol% of IPA from a IPA-water system with z1 = 0.51 and 0.60, respectively. The binary mixture azeotropic point is successfully broken down by calcium chloride salt addition. In pilot plant, salt solution was added near to the top of column and total reflux ratio was applied to enhance mass and heat transfer in salt effect distillation. However, it did not succeeded in recovering high purity of IPA, probably due to errors in the extension of binary data to multi-component systems.

Distillation Engineering

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ISBN 13 :
Total Pages : 544 pages
Book Rating : 4.F/5 ( download)

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Book Synopsis Distillation Engineering by : Reinhard Billet

Download or read book Distillation Engineering written by Reinhard Billet and published by . This book was released on 1979 with total page 544 pages. Available in PDF, EPUB and Kindle. Book excerpt: Partial Table of Contents I. The Thermal Separation of Liquids II. Thermodynamics of Mixtures 1. Definitions and Relationships A. Separability of a Liquid Mixture B. Partial Pressures in Vapor Mixtures C. Evaporation of Liquid Mixtures 2. Types of Mixtures A. Ideal Binary Mixtures B. Nonideal Binary Mixtures C. Ideal Multicomponent Mixtures D. Nonideal Multicomponent Mixtures III. Continuous Rectifiers 1. Mode of Operations 2. Operating Lines A. Enrichment Line B. The Stripping Line 3. Stepwise Separation in Rectifiers A. Theoretical Plates for Separation of Binaries B. The Reflux Ratio in the Separation of Binaries C. Multicomponent Mixtures 4. Column Diameter and Column Throughput 5. Heat Requirements IV. The Batch Still 1. Operation 2. Operating Line and Separation Steps 3. Column Diameter, Column Throughput, and Heat Requirements 4. Time for Separation and Related Variables at Constant Product Concentration A. Molar Vapor Load Constant in Time B. Heat Requirement Constant in Time 5. Separation Time for Variable Heating Area V. The Semicontinuous Still 1. Operation 2. Finding the Operating Lines, the Separation Steps, the Column Load, the Column: Size, and the Heat Demand VI. Engineering Data, Optimization of Costs, and Selection of Column Internals 1. General A. Packing Types B. Plates and Trays 2. Designs and Functions A. Packed Towers B. Plate Columns 3. Evaluation of Rectifying Columns and Best Mode of Operation A. Evaluating and Calculations, Separating Effect, Pressure Loss, Load, Specific Column Volume, and Specific Column Cost B. Numerical Evaluation for Packed Towers C. Quantitative Evaluation for Plate-Type Columns D. Packed Columns versus Tray Columns-Operational Features and Cost E. Special Designs for Vacuum Operation 4. Tests of Full-Size Tower Internals VII. Optimum Separation 1. Optimization of Simple Columns A. The Theory and Its Application B. Quantitative Evaluation 2. Optimization of Multiple Columns A. Duplex Columns: Number of Theoretical Steps, Reflux Ratios, and Vapor Loads B. Vapor Loads of Multiple Columns Subdivided Because of Limited Height C. Optimizing Duplex Rectifiers for Minimum Pressure Loss 3. Optimum Operation of Combined Columns of Different Types Under Special Consideration A. Parallel Arrangement B. Series Arrangement 4. Specialized Operations A. Specialized Hookups and their Calculation B. Rectification in Straight Stripping Columns C. Rectification in Straight Enriching Columns D. Direct Heating of Columns E. Saving Heat in Rectification VIII. Detail Planning of Separating Columns 1. General Viewpoints in the Selection of Column Types 2. Packed Columns Columns 3. Special Packings 4. Plate-Type Columns 5. Pressure Losses in Rectification Columns IX. Partial Distillation 1. Separation of Liquids by Continuous Partial Distillation 2. Separation of Liquids by Discontinuous Partial Distillation X. Partial Condensation 1. Partial Condensation in Dephlegmators 2. Partial Countercurrent Direct Condensation in Columns XI. Laboratory Columns and Pilot Plants 1. Distillation Columns with Miniature Size Packing 2. Transferring Data Gained From Semi-industrial Units to Full-Scale XII. Distillation in Fine and High Vacuum 1. Molecular Distillation 2. Thin-Film Distillation 3. Mechanism of Separation XIII. Components of a Separation Plant 1. Internal Components 2. Heat Exchangers 3. Pumps 4. Measuring and Controls XIV. Use of Computers XV. Distillation and Environmental Protection XVI. Outlook Bibliography Symbols and Units Glossary Index

Distillation Theory and its Application to Optimal Design of Separation Units

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Publisher : Cambridge University Press
ISBN 13 : 9781139455633
Total Pages : 368 pages
Book Rating : 4.4/5 (556 download)

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Book Synopsis Distillation Theory and its Application to Optimal Design of Separation Units by : F. B. Petlyuk

Download or read book Distillation Theory and its Application to Optimal Design of Separation Units written by F. B. Petlyuk and published by Cambridge University Press. This book was released on 2004-10-18 with total page 368 pages. Available in PDF, EPUB and Kindle. Book excerpt: Originally published in 2004, Distillation Theory and Its Application to Optimal Design of Separation Units presents a clear, multidimensional geometric representation of distillation theory that is valid for all distillation column types, splits, and mixtures. This representation answers such fundamental questions as: what are the feasible separation products for a given mixture? What minimum power is required to separate a given mixture? What minimum number of trays is necessary to separate a given mixture at a fixed power input? This book is intended for students and specialists in the design and operation of separation units in the chemical, pharmaceutical, food, wood, petrochemical, oil-refining, and natural gas industries and for software designers.

Encyclopedia of Separation Science

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Publisher :
ISBN 13 :
Total Pages : 582 pages
Book Rating : 4.:/5 (318 download)

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Book Synopsis Encyclopedia of Separation Science by : Michael Cooke

Download or read book Encyclopedia of Separation Science written by Michael Cooke and published by . This book was released on 2000 with total page 582 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Separation of a highly nonideal mixture for solvent recovery

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Publisher : diplom.de
ISBN 13 : 3832463097
Total Pages : 82 pages
Book Rating : 4.8/5 (324 download)

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Book Synopsis Separation of a highly nonideal mixture for solvent recovery by : Andreas Raab

Download or read book Separation of a highly nonideal mixture for solvent recovery written by Andreas Raab and published by diplom.de. This book was released on 2003-01-15 with total page 82 pages. Available in PDF, EPUB and Kindle. Book excerpt: Inhaltsangabe:Abstract: The separation of complex nonideal mixtures is a common problem in the process industries. The solvent recovery is an important task for chemical engineers to minimize burden upon the environment due to exhaustive use of solvents. The recovery of the individual components is complicated by the highly nonideal features of these mixtures. The separation of such highly nonideal mixtures can be limited by the presence of azeotropes, which can create distillation boundaries. These distillation boundaries are forming distillation regions which are difficult to overcome with the standard rectification. Distillation systems for these highly nonideal azeotropic mixtures are particularly difficult to design and to operate in an efficient way. In printing companies often four component mixtures of ethanol, ethyl acetate, isopropyl acetate, and water arise as waste. A separation scheme of multicomponent azeotropic distillation is developed and successfully used for a highly nonideal quaternary mixture. The composition of the mixture in mass percent is ethanol 30%, water 20%, ethyl acetate 25% and isopropyl acetate with 20%. The rest of the mixture (5%) consists of n-propane, isopropane, cyclohexane, and etoxypropane. For the further investigation just the quaternary mixture is examined. Generally, every component should be recovered as pure as possible from the mixture. In the mixture namely five binary and two ternary azeotropes are formed by the components. Based on the synthesis procedure proposed by Rev et al. and Mizsey et al. a new separation technology is developed followed up the vapor-liquid-liquid equilibrium behavior of the mixture. They have recommended a general framework for designing feasible schemes of multicomponent azeotropic distillation. This procedure recommends to study in detail the vapor-liquid-liquid equilibrium data to explore immiscibility regions, azeotropic points, and separatrices for ternary and quaternary regions. On the behalf of the VLLE data the set of feasible separation structures is explored. This procedure is followed and a new separation structure is developed and tested experimentally. First, the quaternary mixture is separated into two ternary mixtures by distillation. The two ternary mixtures containing ethyl acetate, ethanol, water and isopropyl acetate, ethanol, water, respectively. Due to the analogous behavior of the two ternary mixtures similar separation cycles can be designed. The two [...]

Synthesis of Azeotropic Batch Distillation Separation Systems

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ISBN 13 :
Total Pages : 41 pages
Book Rating : 4.:/5 (377 download)

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Book Synopsis Synthesis of Azeotropic Batch Distillation Separation Systems by : Boyd T. Safrit

Download or read book Synthesis of Azeotropic Batch Distillation Separation Systems written by Boyd T. Safrit and published by . This book was released on 1996 with total page 41 pages. Available in PDF, EPUB and Kindle. Book excerpt: Abstract: "Batch distillation has received renewed interest as the market for small volume, high value, specialty chemicals has increased. While batch distillation is more flexible than continuous distillation because the same equipment can be used for several products and operating conditions, batch distillation can be less flexible when azeotropes are present in the mixture to be separated. Azeotropes can form batch distillation regions where the types of feasible separations can be more limited than in continuous distillation. New types of batch column configurations, such as the middle vessel column, can help in the separation of azeotropic mixtures. We show how insights developed for continuous distillation can identify the feasible products and possible column profiles for such a column. We compare extractive distillation using the middle vessel column and a batch rectifying column. While both can often theoretically recover 100% of the pure components from a binary azeotropic mixture, the middle vessel has the benefits of a finite size still pot which is made possible by 'steering' the still composition versus time. We also investigate the operation of the extractive middle vessel column by looking at the sensitivity of a profit function to some of the operational parameters. In order to separate azeotropic mixtures in general, a sequence of batch columns must normally be used. A tool for finding the basic, continuous and batch distillation regions for any mixture is developed in order to synthesize such sequences. This tool, given an initial still composition, can determine the possible products at total reflux and reboil and infinite number of trays for a variety of batch column configurations. We then show how to use such a tool in the synthesis of all possible batch column sequences."

Azeotropic and Extractive Distillation

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Publisher : Krieger Publishing Company
ISBN 13 :
Total Pages : 338 pages
Book Rating : 4.:/5 (319 download)

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Book Synopsis Azeotropic and Extractive Distillation by : Edward Jack Hoffman

Download or read book Azeotropic and Extractive Distillation written by Edward Jack Hoffman and published by Krieger Publishing Company. This book was released on 1964 with total page 338 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Batch Distillation: Design And Operation

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Publisher : World Scientific Publishing Company
ISBN 13 : 1911299026
Total Pages : 416 pages
Book Rating : 4.9/5 (112 download)

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Book Synopsis Batch Distillation: Design And Operation by : Mujtaba Iqbal M

Download or read book Batch Distillation: Design And Operation written by Mujtaba Iqbal M and published by World Scientific Publishing Company. This book was released on 2004-03-29 with total page 416 pages. Available in PDF, EPUB and Kindle. Book excerpt: The batch distillation process has existed for many centuries. It is perhaps the oldest technology for separating or purifying liquid mixtures and is the most frequently used separation method in batch processes. In the last 25 years, with continuous development of faster computers and sophisticated numerical methods, there have been many published works using detailed mathematical models with rigorous physical property calculations and advanced optimisation techniques to address several important issues, such as selection of column configurations, design, operation, off-cut recycling, use of batch distillation in reactive and extractive modes, etc.Batch Distillation: Design and Operation presents excellent, important contributions of many researchers from around the globe, including those of the author and his co-workers./a

Distillation

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ISBN 13 :
Total Pages : 706 pages
Book Rating : 4.:/5 (318 download)

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Book Synopsis Distillation by :

Download or read book Distillation written by and published by . This book was released on 1951 with total page 706 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Distillation and Absorption '97

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Publisher : IChemE
ISBN 13 :
Total Pages : 510 pages
Book Rating : 4.3/5 (91 download)

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Book Synopsis Distillation and Absorption '97 by : Richard Darton

Download or read book Distillation and Absorption '97 written by Richard Darton and published by IChemE. This book was released on 1997 with total page 510 pages. Available in PDF, EPUB and Kindle. Book excerpt: This volume presents reports from the 1997 conference, held in Maastricht, Netherlands. The papers, covering a broad range of topics from the estimation of physical properties to the design and performance of contacting trays, demonstrate the high rate of advance in technology.

Elements of Fractional Distillation

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Publisher : Blatter Press
ISBN 13 : 1443720607
Total Pages : 508 pages
Book Rating : 4.4/5 (437 download)

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Book Synopsis Elements of Fractional Distillation by : Shove Robinson Clark

Download or read book Elements of Fractional Distillation written by Shove Robinson Clark and published by Blatter Press. This book was released on 2008-11 with total page 508 pages. Available in PDF, EPUB and Kindle. Book excerpt: Elements of Fractional Distillation By CLARK SHOVE ROBINSON AND EDWIN RICHARD GLLLILAND. PREFACE TO THE FOURTH EDITION: This book and the early revisions were the result of the efforts of Professor Robinson, and he took an active part in guiding the revision of the previous edition. His death made it necessary to prepare this edition without his helpful guidance and counsel. The present revision differs extensively from the previous edition. The material has been modified to bring it more closely into line with the graduate instruction in distillation at Massachusetts Institute of Technology. Much greater emphasis has been placed on the measurement, prediction, and use of vapor-liquid equilibria because it is believed that this is one of the most serious limitations in design calculations. Greater emphasis has also been placed upon the use of enthalpy balances, and the treatment of batch distillation has been considerably expanded. Unfortunately, the design calculations for this type of operation are still in an unsatisfactory status. Azeotropic and extractive distillation are considered as an extension of conventional multicomponent problems. The sections on column design and column performance have been completely rewritten and increased in scope. In all cases quantitative examples have been given because it has been found that this greatly aids the student in understanding descriptive material. During the last 15 years a large number of design methods have been proposed for multicomponent mixtures, some of which are reviewed in Chapter 12. Most of these do not appear to offer any great advantage over the conventional Sorel method, and it is believed that the law of diminishing returns has been applying in this field for some time. It is hoped that the present edition will stimulate some of these investigators to transfer their efforts to more critical problems, such as vapor-liquid equilibria, batch distillation, transient conditions within the distillation system, and column performance. EDWIN RICHARD GILLILAND CAMBRIDGE, MASS. July, 1960. PREFACE TO THE FIRST EDITION: The subject of fractional distillation has received but scant attention from, writers in the English language since Sidney Young published his book Fractional Distillation in 1903 London. French and German authors have, on the other hand, produced a number of books on the subject, among the more important of which are the following La Rectification et les colonnes rectificatriccs en distillerie, E. Barbet, Paris, 1890 2d ed., 1895. Der Wirkungsweise der Rcctificir und Destillir Apparate, E. Hausbrand, Berlin, 1893 3d ed., 1910. Theorie der Verdampfimg und Verfliissung von gemischcn und der fraktionierten Destination, J. P. Kuenen, Leipzig, 1906. Theorie der Gewinnung und Trennung der atherischen Olc durch Destination, C. von Rechenberg, Leipzig, 1910. La Distillation fractione e et la rectification, Charles Manlier, Paris, 1917. Youngs Fractional Distillation, although a model for its kind, has to do almost entirely with the aspects of the subject as viewed from the chemical laboratory, and there has been literally no work in English available for the engineer and plant operator dealing with the applications of the laboratory processes to the plant. The use of the modern types of distilling equipment is growing at a very rapid rate. Manufacturers of chemicals are learning that they must refine their products in order to market them successfully, and it is often true that fractional distillation offers the most available if not the only way of accomplishing this...

The Effect of Reflux Ratio on the Degree of Separation in Continuous Distillation of Hydrocarbon Mixtures

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ISBN 13 :
Total Pages : 98 pages
Book Rating : 4.:/5 (373 download)

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Book Synopsis The Effect of Reflux Ratio on the Degree of Separation in Continuous Distillation of Hydrocarbon Mixtures by : George C. McFarland

Download or read book The Effect of Reflux Ratio on the Degree of Separation in Continuous Distillation of Hydrocarbon Mixtures written by George C. McFarland and published by . This book was released on 1924 with total page 98 pages. Available in PDF, EPUB and Kindle. Book excerpt:

Distillation: Equipment and Processes

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Publisher : Academic Press
ISBN 13 : 0123868793
Total Pages : 373 pages
Book Rating : 4.1/5 (238 download)

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Book Synopsis Distillation: Equipment and Processes by : Andrzej Gorak

Download or read book Distillation: Equipment and Processes written by Andrzej Gorak and published by Academic Press. This book was released on 2014-06-24 with total page 373 pages. Available in PDF, EPUB and Kindle. Book excerpt: Distillation: Equipment and Processes—winner of the 2015 PROSE Award in Chemistry & Physics from the Association of American Publishers—is a single source of authoritative information on all aspects of the theory and practice of modern distillation, suitable for advanced students and professionals working in a laboratory, industrial plants, or a managerial capacity. It addresses the most important and current research on industrial distillation, including all steps in process design (feasibility study, modeling, and experimental validation), together with operation and control aspects. This volume features an extra focus on distillation equipment and processes. Winner of the 2015 PROSE Award in Chemistry & Physics from the Association of American Publishers Practical information on the newest development written by recognized experts Coverage of a huge range of laboratory and industrial distillation approaches Extensive references for each chapter facilitates further study