Distillation Techniques in the Fruit Spirits Production
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Extraction of Wax from Sorghum Bran •
i EXTRACTION OF WAX FROM SORGHUM BRAN • 1 HSIEN-WEN HSU <& . ***£/ B. S., National Taiwan University, China, 1951 A THESIS » submitted in partial fulfillment of the requirements for the degree MASTER OF SCIENCE - Department of Chemical Engineering KANSAS STATE COLLEGE OF AGRICULTURE AND APPLIED SCIENCE - 1955 » k Lo i~i ii Q^cu^v^Js TABLE OF CONTENTS INTRODUCTION 1 PREVIOUS WORK 3 MATERIALS 6 GLASS SOXHLET EXTRACTION AND ANALYSIS OF WAX AND OIL IN MISCELLA 7 Procedure of Using Soxhlet Extractor 7 Separation of Wax from Oil by the Acetone Method.. 8 Summary of Results 9 PILOT PLANT EXTRACTION 15 SEPARATION OF WAX AND OIL 16 Effect of Temperature in the Acetone Method 16 Urea Complex Method of Separation. 17 Theory 17 Experimental Procedure 22 Summary of Results 26 COST ESTIMATION OF A WAX RECOVERY PLANT 29 DISCUSSION 30 CONCLUSIONS 35 ACKNOWLEDGMENTS 36 BIBLIOGRAPHY 37 APPENDIX 39 INTRODUCTION i One of the functions of the Agricultural Experiment Station is the never ending search for means of better and fuller utilization of the agri- cultural products that are of particular interest in the state of Kansas. In line with this broad objective, the extraction of economically valuable lipid materials from the sorghum bran has been studied in several theses in the Departments of Chemical Engineering and Chemistry in recent years. Generally the emphasis has b. en placed upon either the chemical and physical properties of these lipides or the equipment design and performance for the solvent ex- traction operation. A brief review of the previous work is presented in the ensuing section. -
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. -
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. -
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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 65 Chem 355 Jasperse DISTILLATION
Distillation 65 Chem 355 Jasperse DISTILLATION Background Distillation is a widely used technique for purifying liquids. The basic distillation process involves heating a liquid such that liquid molecules vaporize. The vapors produced are subsequently passed through a water-cooled condenser. Upon cooling, the vapor returns to it’s liquid phase. The liquid can then be collected. The ability to separate mixtures of liquids depends on differences in volatility (the ability to vaporize). For separation to occur, the vapor that is condensed and collected must be more pure than the original liquid mix. Distillation can be used to remove a volatile solvent from a nonvolatile product; to separate a volatile product from nonvolatile impurities; or to separate two or more volatile products that have sufficiently different boiling points. Vaporization and Boiling When a liquid is placed in a closed container, some of the molecules evaporate into any unoccupied space in the container. Evaporation, which occurs at temperatures below the boiling point of a compound, involves the transition from liquid to vapor of only those molecules at the liquid surface. Evaporation continues until an equilibrium is reached between molecules entering and leaving the liquid and vapor states. The pressure exerted by these gaseous molecules on the walls of the container is the equilibrium vapor pressure. The magnitude of this vapor pressure depends on the physical characteristics of the compound and increases as temperature increases. In an open container, equilibrium is never established, the vapor can simply leave, and the liquid eventually disappears. But whether in an open or closed situation, evaporation occurs only from the surface of the liquid. -
Standard Operating Procedures
Standard Operating Procedures 1 Standard Operating Procedures OVERVIEW In the following laboratory exercises you will be introduced to some of the glassware and tech- niques used by chemists to isolate components from natural or synthetic mixtures and to purify the individual compounds and characterize them by determining some of their physical proper- ties. While working collaboratively with your group members you will become acquainted with: a) Volumetric glassware b) Liquid-liquid extraction apparatus c) Distillation apparatus OBJECTIVES After finishing these sessions and reporting your results to your mentor, you should be able to: • Prepare solutions of exact concentrations • Separate liquid-liquid mixtures • Purify compounds by recrystallization • Separate mixtures by simple and fractional distillation 2 EXPERIMENT 1 Glassware Calibration, Primary and Secondary Standards, and Manual Titrations PART 1. Volumetric Glassware Calibration Volumetric glassware is used to either contain or deliver liquids at a specified temperature. Glassware manufacturers indicate this by inscribing on the volumetric ware the initials TC (to contain) or TD (to deliver) along with the calibration temperature, which is usually 20°C1. Volumetric glassware must be scrupulously clean before use. The presence of streaks or droplets is an indication of the presence of a grease film. To eliminate grease from glassware, scrub with detergent solution, rinse with tap water, and finally rinse with a small portion of distilled water. Volumetric flasks (TC) A volumetric flask has a large round bottom with only one graduation mark positioned on the long narrow neck. Graduation Mark Stopper The position of the mark facilitates the accurate and precise reading of the meniscus. If the flask is used to prepare a solution starting with a solid compound, add small amounts of sol- vent until the entire solid dissolves. -
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 .. -
Alembic Pot Still
ALEMBIC POT STILL INSTRUCTION MANUAL CAN BE USED WITH THE GRAINFATHER OR T500 BOILER SAFETY Warning: This system produces a highly flammable liquid. PRECAUTION: • Always use the Alembic Pot Still System in a room with adequate ventilation. • Never leave the Alembic Pot Still system unattended when operating. • Keep the Alembic Pot Still system away from all sources of ignition, including smoking, sparks, heat, and open flames. • Ensure all other equipment near to the Alembic Pot Still system or the alcohol is earthed. • A fire extinguishing media suitable for alcohol should be kept nearby. This can be water fog, fine water spray, foam, dry powder, carbon dioxide, sand or dolomite. • Do not boil dry. In the event the still is boiled dry, reset the cutout button under the base of the still. In the very unlikely event this cutout fails, a fusible link gives an added protection. IN CASE OF SPILLAGE: • Shut off all possible sources of ignition. • Clean up spills immediately using cloth, paper towels or other absorbent materials such as soil, sand or other inert material. • Collect, seal and dispose accordingly • Mop area with excess water. CONTENTS Important points before getting started ............................................................................... 3 Preparing the Alembic Pot Still ................................................................................................. 5 Distilling a Whiskey, Rum or Brandy .......................................................................................7 Distilling neutral -
Laboratory Rectifying Stills of Glass 2
» LABORATORY RECTIFYING STILLS OF GLASS 2 By Johannes H. Bruun 3 and Sylvester T. Schicktanz 3 ABSTRACT A complete description is given of a set of all-glass rectifying stills, suitable for distillation at pressures ranging from atmospheric down to about 50 mm. The stills are provided with efficient bubbling-cap columns containing 30 to 60 plates. Adiabatic conditions around the column are maintained by surrounding it with a jacket provided with a series of independent electrical heating units. Suitable means are provided for adjusting or maintaining the reflux ratio at the top of the column. For the purpose of conveniently obtaining an accurate value of the true boiling points of the distillates a continuous boiling-point apparatus is incor- porated in the receiving system. An efficient still of the packed-column type for distillations under pressures less than 50 mm is also described. Methods of operation and efficiency tests are given for the stills. CONTENTS Page I. Introduction 852 II. General features of the still assembly 852 III. Still pot 853 IV. Filling tube and heater for the still pot 853 V. Rectifying column 856 1. General features 856 2. Large-size column 856 3. Medium-size column 858 4. Small-size column 858 VI. Column jacket 861 VII. Reflux regulator 861 1. With variable reflux ratio 861 2. With constant reflux ratio 863 VIII. The continuous boiling-point apparatus 863 IX. Condensers and receiver 867 X. The mounting of the still 867 XI. Manufacture and transportation of the bubbling-cap still 870 XII. Operation of the bubbling-cap still 870 XIII. -
Building a Home Distillation Apparatus
BUILDING A HOME DISTILLATION APPARATUS A Step by Step Guide Building a Home Distillation Apparatus i BUILDING A HOME DISTILLATION APPARATUS Foreword The pages that follow contain a step-by-step guide to building a relatively sophisticated distillation apparatus from commonly available materials, using simple tools, and at a cost of under $100 USD. The information contained on this site is directed at anyone who may want to know more about the subject: students, hobbyists, tinkers, pure water enthusiasts, survivors, the curious, and perhaps even amateur wine and beer makers. Designing and building this apparatus is the only subject of this manual. You will find that it confines itself solely to those areas. It does not enter into the domains of fermentation, recipes for making mash, beer, wine or any other spirits. These areas are covered in detail in other readily available books and numerous web sites. The site contains two separate design plans for the stills. And while both can be used for a number of distillation tasks, it should be recognized that their designs have been optimized for the task of separating ethyl alcohol from a water-based mixture. Having said that, remember that the real purpose of this site is to educate and inform those of you who are interested in this subject. It is not to be construed in any fashion as an encouragement to break the law. If you believe the law is incorrect, please take the time to contact your representatives in government, cast your vote at the polls, write newsletters to the media, and in general, try to make the changes in a legal and democratic manner. -
Batch Distillation of Spirits: Experimental Study and Simulation
Research article Received: 5 April 2018 Revised: 11 January 2019 Accepted: 15 January 2019 Published online in Wiley Online Library (wileyonlinelibrary.com) DOI 10.1002/jib.560 Batch distillation of spirits: experimental study and simulation of the behaviour of volatile aroma compounds Adrien Douady,1 Cristian Puentes,1 Pierre Awad1,2 and Martine Esteban-Decloux1* This paper focuses on the behaviour of volatile compounds during batch distillation of wine or low wine, in traditional Charentais copper stills, heated with a direct open flame at laboratory (600 L) and industrial (2500 L) scale. Sixty-nine volatile compounds plus ethanol were analysed during the low wine distillation in the 600 L alembic still. Forty-four were quantified and classified according to their concentration profile in the distillate over time and compared with previous studies. Based on the online re- cording of volume flow, density and temperature of the distillate with a Coriolis flowmeter, distillation was simulated with ProSim® BatchColumn software. Twenty-six volatile compounds were taken into account, using the coefficients of the ‘Non- Random Two Liquids’ model. The concentration profiles of 18 compounds were accurately represented, with slight differences in the maximum concentration for seven species together with a single compound that was poorly represented. The distribution of the volatile compounds in the four distillate fractions (heads, heart, seconds and tails) was well estimated by simulation. Fi- nally, data from wine and low wine distillations in the large-scale alembic still (2500 L) were correctly simulated, suggesting that it was possible to adjust the simulation parameters with the Coriolis flowmeter recording and represent the concentration pro- files of most of the quantifiable volatile compounds. -
Fractional Distillation (Ideal) 1-Propanol/2-Propanol at 760 Torr
Statistical Molecular Thermodynamics Christopher J. Cramer Video 10.7 Azeotropes and Immiscible Phases Fractional Distillation (Ideal) 1-propanol/2-propanol at 760 torr (from Video 10.5) bp as a function of composition x1−propanol(Solution) y1−propanol (Vapor) At 90 °C (between the two pure component boiling points) € the composition of the liquid is 59 mol% 1-propanol (point a) and the vapor is 45 mol% 1-propanol (point b) Fractional distillation: vapor is condensed and revaporized many times a to b to c to d to ... and finally you get to the pure lower boiling component at the top (the coolest point) of a distillation head! Fractional Distillation (Non-Ideal) benzene/ethanol at 760 torr Using Dalton’s/Raoult’s laws: * P2 x2P2 b b y = = a a 2 760 torr lim x2→1 760 torr d c d c and Dalton’s/Henry’s laws: f e e P2 x2kH,2 y2 = = 760 torr lim x2→0 760 torr bp as a function of composition Deviation from ideality permits the vapor phase to be enriched in either component depending on liquid composition. Distillation of benzene-rich mixture Distillation of ethanol-rich mixture Fractional distillation: vapor is condensed and revaporized many times a to b to c to d to e to f, but, irrespective of initial composition, ultimately an azeotropic composition is reached (about 55:45 above) that cannot be further separated by distillation! Self-assessment What purification can be accomplished for a liquid mixture that is not already at the azeotropic composition? Self-assessment Explained If not already at the azeotropic composition, the azeotrope at the top of b b a a the distillation head will be carrying away a greater fraction of one component than d is present in the liquid.