Distillation 1 Distillation
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
Multicomponent Distillation
01/12/2009 Multicomponent distillation F. Grisafi 1 01/12/2009 Introduction The problem of determining the stage and reflux requitirements for multicomponen t distill a tions ismuch more complex than for binary mixtures. With a multicomponent mixture, fixing one component composition does not uniquely determine theother component compositions and the stage temperature. Also when the feed contains more than two components it is not possible to specify the complete composition of the top and bottom products independently. The separation between the top and bottom products is usually specified by setting limits on two "key components", between which it is desired to make the separation. 2 01/12/2009 Calculation procedure The normal procedure for a typical problem is to solve the MESH (Material balance, Equilibrium, Summation and Heat) balance equations stage-by-stage, from the top and bottom of the column toward the feed point. For such a calculation to be exact, the compositions obtained from both the bottom-up and top-down calculations must mesh at the feed point and mesh the feed composition. The calculated compositions will depend on the compositions assumed for the top and bottom products at the commencement of the calculations. Though it ispossibletomatch the key components, theother components will not match unless the designer was particularly fortunate in choosing the trial top and bottom compositions. 3 01/12/2009 Calculation procedure For a comppyletely rigorous solution the compositions must be adjusted and the calculations repeated until a satisfactory match at the feed point is obtained by iterative trial-and-error calculations. Clearly, the greater the number of components, the more difficult the problem. -
The Separation of Three Azeotropes by Extractive Distillation by An-I Yeh A
The separation of three azeotropes by extractive distillation by An-I Yeh A thesis submitted in partial fulfillment of the requirement for the degree of Master of Science in Chemical Engineering Montana State University © Copyright by An-I Yeh (1983) Abstract: Several different kinds of extractive distillation agents were investigated to affect the separation of three binary liquid mixtures, isopropyl ether - acetone, methyl acetate - methanol, and isopropyl ether - methyl ethyl ketone. Because of the small size of the extractive distillation column, relative volatilities were assumed constant and the Fenske equation was used to calculate the relative volatilities and the number of minimum theoretical plates. Dimethyl sulfoxide was found to be a good extractive distillation agent. Extractive distillation when employing a proper agent not only negated the azeotropes of the above mixtures, but also improved the efficiency of separation. This process could reverse the relative volatility of isopropyl ether and acetone. This reversion was also found in the system of methyl acetate and methanol when nitrobenzene was the agent. However, normal distillation curves were obtained for the system of isopropyl ether and methyl ethyl ketone undergoing extractive distillation. In the system of methyl acetate and methanol, the relative volatility decreased as the agents' carbon number increased when glycols were used as the agents. In addition, the oxygen number and the locations of hydroxyl groups in the glycols used were believed to affect the values of relative volatility. An appreciable amount of agent must be maintained in the column to affect separation. When dimethyl sulfoxide was an agent for the three systems studied, the relative volatility increased as the addition rate increased. -
Development of a Process for N-Butanol Recovery from Abe
937 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 74, 2019 The Italian Association of Chemical Engineering Online at www.cetjournal.it Guest Editors: Sauro Pierucci, Jiří Jaromír Klemeš, Laura Piazza Copyright © 2019, AIDIC Servizi S.r.l. ISBN 978-88-95608-71-6; ISSN 2283-9216 DOI: 10.3303/CET1974157 Development of a Process for N-Butanol Recovery from Abe Wastewater Streams by Membrane Technology * Marco Stoller , Marco Bravi, Paola Russo, Roberto Bubbico, Barbara Mazzarotta Sapienza University of Rome, Dept. of Chemical Materials Environmental Engineering, Via Eudossiana 18, 00184 Rome, Italy [email protected] The aceton-butyl-ethanolic fermentation process (ABE) is a biotechnological process that leads to the production of acetone, n-butanol and ethanol (ABE compounds) from glucose sources and amides by use of certain biomasses. The process was developed initially during the middle of the last century and suffers from decline due to the greater petrochemical production of products and the lowering of the costs of the sector. Nowadays, the ABE process is regaining great interest because the fraction with the highest concentration, i.e. n-butanol, is an excellent constituent for biofuels. The ABE process has been optimized over time to obtain maximum yields of n-butanol, but the problem of separating and concentrating the butanol in the outlet stream of the ABE process persists. To allow an adequate use, often distillation by use of more columns is required. Moreover, the contained biomasses and suspended solids, in high quantity, must be eliminated, leading to overall high treatment costs. This work will report the main idea and some preliminary experimental results for the development and application of a process based on membrane technologies, to separate and concentrate the butanol from ABE process streams to sensibly reduce the difficulty to perform a final distillation. -
Innovation in Continuous Rectification for Tequila Production
processes Communication Innovation in Continuous Rectification for Tequila Production Estarrón-Espinosa Mirna, Ruperto-Pérez Mariela, Padilla-de la Rosa José Daniel * and Prado-Ramírez Rogelio * Centro de Investigación y Asistencia en Tecnología y Diseño del Estado de Jalisco (CIATEJ), Av. Normalistas No. 800, C.P. 44720 Guadalajara, Jalisco, Mexico; [email protected] (E.-E.M.); [email protected] (R.-P.M.) * Correspondence: [email protected] (P.-d.l.R.J.D.); [email protected] (P.-R.R.); Tel.: +33-33455200 (P.-d.l.R.J.D.) Received: 23 March 2019; Accepted: 6 May 2019; Published: 14 May 2019 Abstract: In this study, a new process of continuous horizontal distillation at a pilot level is presented. It was applied for the first time to the rectification of an ordinario fraction obtained industrially. Continuous horizontal distillation is a new process whose design combines the benefits of both distillation columns, in terms of productivity and energy savings (50%), and distillation stills in batch, in terms of the aromatic complexity of the distillate obtained. The horizontal process of continuous distillation was carried out at the pilot level in a manual mode, obtaining five accumulated fractions of distillate that were characterized by gas chromatography (GC-FID). The tequila obtained from the rectification process in this new continuous horizontal distillation process complies with the content of methanol and higher alcohols regulated by the Official Mexican Standard (NOM-006-SCFI-2012). Continuous horizontal distillation of tequila has potential energy savings of 50% compared to the traditional process, besides allowing products with major volatile profiles within the maximum limits established by the regulation for this beverage to be obtained. -
Page2 Sidebar 1.Pdf
Headquarters & Forge Americas Office [email protected] [email protected] +49 (0) 7161 / 97830 215.242.6806 +49 (0) 7161 / 978321 fax fax 215.701.9725 artisan distilling systems 600 liter whiskey still the fine art of distillery technology Germany’s oldest distillery fabricator, since 1869, combining traditional family craftsmanship with leading eau-de-vie distillery innovations and technologies. Meticulously custom-crafted artisan copper pot still systems for all the great distilling traditions, and efficient continuous plants, grappa distillery in copper and stainless steel, for all capacities and applications: 450 liter artisan pot stills – brandy & vodka vodka, whiskey, eaux-de-vie, brandy, rum, gin, grappa, tequila, aguardientes… 1000 liter artisan vodka system 650 liter system with CADi automation continuous mash stripping column C. CARL Ziegelstraße 21 Americas Office Brewing & Distilling Ing. GmbH D-73033 Göppingen PO Box 4388 Technologies Corp. www.christiancarl.com Germany Philadelphia, PA 19118-8388 www.brewing-distilling.com CARL artisan distillery systems the fine art of distillery technology CARL custom-builds each distillery to order in our family shop near Stuttgart in Swabia, with the attention and care of crafting a finely- tuned instrument. All-the-while, we stay focused on the continued development of our distillery technology. There are always new ideas and realizations, such our the in-house developed CARL CADi distillery automation or our patented aroma bubble plate technologies, Our innovations have fostered CARL’s nearly 140 years of family tradition and experience as Germany’s oldest and most respected distillery fabricator, with thousands of successful commissions worldwide. form and function Our diverse customers, from small farmers to winemakers to brewers to large spirits houses, show great enthusiasm and appreciation for the aesthetics and functionality of a CARL distillery: its design, its form, classic and intuitively easy to understand, clear in conception. -
Distillation 6
CHAPTER Energy Considerations in Distillation 6 Megan Jobson School of Chemical Engineering and Analytical Science, The University of Manchester, Manchester, UK CHAPTER OUTLINE 6.1 Introduction to energy efficiency ....................................................................... 226 6.1.1 Energy efficiency: technical issues................................................... 227 6.1.1.1 Heating.................................................................................... 227 6.1.1.2 Coolingdabove ambient temperatures...................................... 229 6.1.1.3 Coolingdbelow ambient temperatures ...................................... 230 6.1.1.4 Mechanical or electrical power.................................................. 232 6.1.1.5 Summarydtechnical aspects of energy efficiency ..................... 233 6.1.2 Energy efficiency: process economics............................................... 233 6.1.2.1 Heating.................................................................................... 233 6.1.2.2 Cooling..................................................................................... 235 6.1.2.3 Summarydprocess economics and energy efficiency ............... 237 6.1.3 Energy efficiency: sustainable industrial development........................ 237 6.2 Energy-efficient distillation ............................................................................... 237 6.2.1 Energy-efficient distillation: conceptual design of simple columns...... 238 6.2.1.1 Degrees of freedom in design .................................................. -
Evaluation of Azeotropic Dehydration for the Preservation of Shrimp. James Edward Rutledge Louisiana State University and Agricultural & Mechanical College
Louisiana State University LSU Digital Commons LSU Historical Dissertations and Theses Graduate School 1969 Evaluation of Azeotropic Dehydration for the Preservation of Shrimp. James Edward Rutledge Louisiana State University and Agricultural & Mechanical College Follow this and additional works at: https://digitalcommons.lsu.edu/gradschool_disstheses Recommended Citation Rutledge, James Edward, "Evaluation of Azeotropic Dehydration for the Preservation of Shrimp." (1969). LSU Historical Dissertations and Theses. 1689. https://digitalcommons.lsu.edu/gradschool_disstheses/1689 This Dissertation is brought to you for free and open access by the Graduate School at LSU Digital Commons. It has been accepted for inclusion in LSU Historical Dissertations and Theses by an authorized administrator of LSU Digital Commons. For more information, please contact [email protected]. This dissertation has been 70-9089 microfilmed exactly as received RUTLEDGE, James Edward, 1941- EVALUATION OF AZEOTROPIC DEHYDRATION FOR THE PRESERVATION OF SHRIMP. The Louisiana State University and Agricultural and Mechanical College, PhJD., 1969 Food Technology University Microfilms, Inc., Ann Arbor, Michigan Evaluation of Azeotropic Dehydration for the Preservation of Shrimp A Dissertation Submitted to the Graduate Faculty of the Louisiana State University and Agricultural and Mechanical College in partial fulfillment of the requirements for the degree of Doctor of Philosophy in The Department of Food Science and Technology by James Edward Rutledge B.S., Texas A&M University, 1963 M.S., Texas A&M University, 1966 August, 1969 ACKNOWLEDGMENT The author wishes to express his sincere appreciation to his major professor, Dr, Fred H. Hoskins, for the guidance which he supplied not only in respect to this dissertation but also in regard to the author’s graduate career at Louisiana State University, Gratitude is also extended to Dr. -
Alchemist's Handbook-First Edition 1960 from One to Ten
BY THE SAME AUTHOR wqt Drei NoveIlen (German) 1932 The Alchemist's Handbook-First Edition 1960 From One to Ten . .. .. 1966 Alrqtuttaf!i Praxis Spagyrica Philosophica 1966 The Seven Rays of the Q.B.L.-First Edition 1968 Praetische Alchemie irn Zwanzigsten Jahrundert 1970 ~aubhnnk (Practical Alchemy in the 20th Century-German) Der Mensch und die kosmischen Zyklen (German) 1971 (Manual for Practical Laboratory Alchemy) Men and the Cycles of the Universe 1971 Von Eins bis Zehn (From One to Ten-German) 1972 El Hombre y los Ciclos del Universo (Spanish) 1972 by Die Sieben Strahlen der Q.B.L. 1973 (The Seven Rays of the Q.B.L.-German) FRATER ALBERTUS SAMUEL WEISER New York CONTENTS Foreword 6 Preface to the First Edition 10 Preface to the Second Revised Edition 13 Chapter I Introduction to Alchemy 14 Samuel Weiser, Inc. Chapter 11 740 Broadway The Lesser Circulation 24 New York, N.Y. 10003 Chapter III First Published 1960 The Herbal Elixir Revised Edition 1974 Chapter IV Third Printing 1978 Medicinal Uses 43 Chapter V © 1974 Paracelsus Research Society Herbs and Stars 47 Salt Lake City, Utah, U.S.A. Chapter VI Symbols in Alchemy 56 ISBN 0 87728 181 5 Chapter VII Wisdom of the Sages 65 Conclusion 100 Alchemical Manifesto 120 ILLUSTRATIONS On the Way to the Temple 5 Soxhlet Extractor 34 Basement Laboratory 41 Essential Equipment 42 Printed in U.S.A. by Qabalistic Tree of Life 57 NOBLE OFFSET PRINTERS, INC. NEW YORK, N.Y. 10003 Alchemical Signs 58 ORIGINAL OIL PAINTING AT PARACELSUS RESEARCH SOCIETY .. -
Laval University
LAVAL UNIVERSITY FACULTY OF FORESTRY AND GEOMATICS Department of Wood and Forest Sciences Sponsored by the International Development Center (IDRC) Ottawa, Canada “The Hidden World that Feeds Us: the Living Soil” Seminars given at the International Institute for Trropical Agriculture (ITA) Univeristy of Ibadan, Nigeria at the International Centre of Research in Agroforestry (ICRAF) Nairobi, Kenya and at the Ukrainian Academy of Agricultural Sciences Kiev, Ukraine by Professor Gilles Lemieux Department of Wood and Forestry Science ORIGINAL FRENCH PUBLICATION Nº 59b http://forestgeomat.ffg.ulaval.ca/brf/ edited by Coordination Group on Ramial Wood Depatment of Wood and Forestry Science Québec G1K 7P4 QUÉBEC CANADA TABLE OF CONTENTS I. A brief history: the evolution of ecosystems and man’s anthropocentric behaviour 1 II. The importance of the forest in tropical climates 2 III. The basic composition of wood 3 1. Lignin and its derivatives and their role in doil dynamic 5 IV. Stem wood and ramial wood 6 1. Stem wood and its lignin 6 2. Ramial wood and its lignin 6 3. Agricultural and forestry trials using ramial wood 7 V. “Organic Matter”, one of the basic principles in agriculture 9 1. Some a posteriori thoughts 10 2. The rationale for chipping 10 3. More like a food than a fertilizer 11 4. The principles behind chipping 11 VI. Lignin 13 1.The nutrients question 14 2.The biological cycling of water in tropical climates 15 3.“Chemical” nutrients 15 4.Nitrogen 15 5.Phosphorus 16 VII. A tentative theory 17 1.Too much or too little water 17 2.The soil-structuring role of lignin 17 3.The role of trophic web 18 4.Living beyond the soil’s chemical constraints 18 5.The major cause of tropical soils degradation. -
A Case Study on Separation of IPA-Water Mixture by Extractive Distillation Using Aspen Plus
International Journal of Advanced Technology and Engineering Exploration, Vol 3(24) ISSN (Print): 2394-5443 ISSN (Online): 2394-7454 Research Article http://dx.doi.org/10.19101/IJATEE.2016.324004 A case study on separation of IPA-water mixture by extractive distillation using aspen plus Sarita Kalla, Sushant Upadhyaya*, Kailash Singh, Rajeev Kumar Dohare and Madhu Agarwal Department of Chemical Engineering, Malaviya National Institute of Technology, Jaipur, India ©2016 ACCENTS Abstract Extractive distillation is one of the popular methods being leveraged to separate isopropyl alcohol (IPA) from water present in waste stream in semi-conductor industries. In this context, the paper aims to carry out simulation study for separation of isopropyl alcohol-water azeotrope mixture using ethylene glycol as entrainer. In particular, temperature, pressure and concentration profile has been studied. Aspen plus® (version 8.8) has been used as simulation tool and optimum number of stages for the simulation turns out to be 42. The results show that top of the column contains IPA of 99.974 mol % purity and bottom product contains water-ethylene glycol mixture. Moreover, sensitivity analysis for different parameters and analysis of residue curve for ternary system have been also performed. Keywords IPA-water, Extractive distillation, Simulation, Entrainer. 1. Introduction 2. Process simulation Isopropyl alcohol is generally used as the cleaning 2.1 Thermodynamic model agent and solvent in chemical industries. Because of Thermodynamic model is used to describe phase its cleaning property it is also known as rubbing equilibria properties of the system. For the design of alcohol. IPA is soluble in water and it forms chemical separation operations the phase equilibrium azeotrope with water at temperature 80.3-80.4 0C. -
The Destructive Distillation of Pine Sawdust
Scholars' Mine Bachelors Theses Student Theses and Dissertations 1903 The destructive distillation of pine sawdust Frederick Hauenstein Herbert Arno Roesler Follow this and additional works at: https://scholarsmine.mst.edu/bachelors_theses Part of the Mining Engineering Commons Department: Mining Engineering Recommended Citation Hauenstein, Frederick and Roesler, Herbert Arno, "The destructive distillation of pine sawdust" (1903). Bachelors Theses. 238. https://scholarsmine.mst.edu/bachelors_theses/238 This Thesis - Open Access is brought to you for free and open access by Scholars' Mine. It has been accepted for inclusion in Bachelors Theses by an authorized administrator of Scholars' Mine. This work is protected by U. S. Copyright Law. Unauthorized use including reproduction for redistribution requires the permission of the copyright holder. For more information, please contact [email protected]. FOR THE - ttl ~d IN SUBJECT, ••The Destructive Distillation of P ine Sawdust:• F . HAUENSTEIN AND H . A. ROESLER. CLASS OF 1903. DISTILLATION In pine of the South, the operation of m.ills to immense quanti waste , such and sawdust.. The sawdust especially, is no practical in vast am,ounte; very difficult to the camp .. s :ls to util the be of commercial .. folloWing extraction turpentine .. of the acid th soda and treat- products .. t .. the t.he turpentine to in cells between , or by tissues to alcohol, a soap which a commercial t this would us too the rd:- hydrochloric was through supposition being that it d form & pinene hydro- which produced~ But instead the hydrochl , a dark unl<:nown compound was The fourth experiment, however, brought out a number of possibilities, a few of Which have been worked up. -
Review of Extractive Distillation. Process Design, Operation
Review of Extractive Distillation. Process design, operation optimization and control Vincent Gerbaud, Ivonne Rodríguez-Donis, Laszlo Hegely, Péter Láng, Ferenc Dénes, Xinqiang You To cite this version: Vincent Gerbaud, Ivonne Rodríguez-Donis, Laszlo Hegely, Péter Láng, Ferenc Dénes, et al.. Review of Extractive Distillation. Process design, operation optimization and control. Chemical Engineering Research and Design, Elsevier, 2019, 141, pp.229-271. 10.1016/j.cherd.2018.09.020. hal-02161920 HAL Id: hal-02161920 https://hal.archives-ouvertes.fr/hal-02161920 Submitted on 21 Jun 2019 HAL is a multi-disciplinary open access L’archive ouverte pluridisciplinaire HAL, est archive for the deposit and dissemination of sci- destinée au dépôt et à la diffusion de documents entific research documents, whether they are pub- scientifiques de niveau recherche, publiés ou non, lished or not. The documents may come from émanant des établissements d’enseignement et de teaching and research institutions in France or recherche français ou étrangers, des laboratoires abroad, or from public or private research centers. publics ou privés. Open Archive Toulouse Archive Ouverte OATAO is an open access repository that collects the work of Toulouse researchers and makes it freely available over the web where possible This is an author’s version published in: http://oatao.univ-toulouse.fr/239894 Official URL: https://doi.org/10.1016/j.cherd.2018.09.020 To cite this version: Gerbaud, Vincent and Rodríguez-Donis, Ivonne and Hegely, Laszlo and Láng, Péter and Dénes, Ferenc and You, Xinqiang Review of Extractive Distillation. Process design, operation optimization and control. (2018) Chemical Engineering Research and Design, 141.