Innovation in a Continuous System of Distillation by Steam to Obtain Essential Oil from Persian Lime Juice (Citrus Latifolia Tanaka)

Total Page:16

File Type:pdf, Size:1020Kb

Load more

molecules Article Innovation in a Continuous System of Distillation by Steam to Obtain Essential Oil from Persian Lime Juice (Citrus latifolia Tanaka) José Daniel Padilla-de la Rosa 1 , Magaly Dyanira Manzano-Alfaro 2, Jaime Rosalío Gómez-Huerta 3, Enrique Arriola-Guevara 2, Guadalupe Guatemala-Morales 4,* , Anaberta Cardador-Martínez 5,* and Mirna Estarrón-Espinosa 1,* 1 Unidad Zapopan, Centro de Investigación y Asistencia en Tecnología y Diseño del Estado de Jalisco (CIATEJ), Av. Camino Arenero No. 1227, Col. El Bajío, Guadalajara C.P. 45019, Mexico; [email protected] 2 Departamento de Ingeniería Química, CUCEI, Universidad de Guadalajara, Blvd. Marcelino García Barragán #1421, esq. Calzada Olímpica, Guadalajara C.P. 44430, Mexico; [email protected] (M.D.M.-A.); [email protected] (E.A.-G.) 3 Departamento de Química, CUCEI, Universidad de Guadalajara, Blvd. Marcelino García Barragán #1421, esq. Calzada Olímpica, Guadalajara C.P. 44430, Mexico; [email protected] 4 Unidad Normalistas, Centro de Investigación y Asistencia en Tecnología y Diseño del Estado de Jalisco (CIATEJ), Av. Normalistas No. 800, Guadalajara C.P. 44720, Mexico 5 Escuela de Ingeniería y Ciencias, Tecnologico de Monterrey, Epigmenio González 500 Fracc. San Pablo, Querétaro C.P. 76130, Mexico Citation: Padilla-de la Rosa, J.D.; * Correspondence: [email protected] (G.G.-M.); [email protected] (A.C.-M.); Manzano-Alfaro, M.D.; [email protected] (M.E.-E.) Gómez-Huerta, J.R.; Arriola-Guevara, E.; Guatemala-Morales, G.; Abstract: The citrus industry is one of the most important economic areas within the global agricul- Cardador-Martínez, A.; tural sector. Persian lime is commonly used to produce lime juice and essential oil, which are usually Estarrón-Espinosa, M. Innovation in a obtained by batch distillation. The aim of this work was to validate a patented continuous steam dis- Continuous System of Distillation by tillation process and to both physically and chemically characterize the volatile fractions of essential Steam to Obtain Essential Oil from Persian lime oil. Prior to distillation, lime juice was obtained by pressing the lime fruit. Afterwards, Persian Lime Juice (Citrus latifolia the juice was subjected to a continuous steam distillation process by varying the ratio of distillate Tanaka). Molecules 2021, 26, 4172. flow to feed flow (0.2, 0.4, and 0.6). The distillate oil fractions were characterized by measuring their https://doi.org/10.3390/ density, optical rotation, and refractive index. Gas chromatography GC-FID was used to analyze the molecules26144172 chemical compositions of the oil fractions. The process of continuous steam distillation presented high oil recovery efficiencies (up to 90%) and lower steam consumption compared to traditional Academic Editor: Laura De Martino batch process distillation since steam consumption ranged from 32 to 60% for different steam levels. Received: 11 June 2021 Moreover, a reduction in process time was observed (from 8 to 4 h). The oil fractions obtained via Accepted: 3 July 2021 continuous steam distillation differed significantly in their composition from the parent compounds Published: 9 July 2021 and the fractions. Publisher’s Note: MDPI stays neutral Keywords: essential oils; distillation by steam; continuous processes with regard to jurisdictional claims in published maps and institutional affil- iations. 1. Introduction Citrus is the most abundant crop of fruit trees around the world, with annual pro- duction in 2015 totaling approximately 130,947 million tons. The main citrus fruits grown Copyright: © 2021 by the authors. globally are oranges, mandarins, lemons, limes, and grapefruits. Brazil, China, India, Licensee MDPI, Basel, Switzerland. Mexico, Spain, and the USA produce over two-thirds of the world’s citrus fruits [1]. In This article is an open access article 2017, the worldwide production of acid lime fruit was 17,218,173 tons, among which Mex- distributed under the terms and ico contributed 2,528,174 tons and was thus considered the main producer of lime fruit, conditions of the Creative Commons comprising 14.7% of the total production [2]. Attribution (CC BY) license (https:// creativecommons.org/licenses/by/ 4.0/). Molecules 2021, 26, 4172. https://doi.org/10.3390/molecules26144172 https://www.mdpi.com/journal/molecules Molecules 2021, 26, x 2 of 19 Molecules 2021, 26, 4172 2 of 18 1.1. Industrial Use of Lemons 1.1. IndustrialFor many Use years, of Lemons the citrus processing industry has focused on the production of juices and essential oils. It was estimated that 33% of citrus harvested in the world is used For many years, the citrus processing industry has focused on the production of juices to produce juices [3]. In the processing of citrus fruits (orange, lemon, lime, grapefruit, and essential oils. It was estimated that 33% of citrus harvested in the world is used to etc.) for juice and essential oil extractions, peels represent between 50 and 65% of the total produce juices [3]. In the processing of citrus fruits (orange, lemon, lime, grapefruit, etc.) weight of the fruits and remain the primary byproduct [4]. This solid residue, referred to for juice and essential oil extractions, peels represent between 50 and 65% of the total as citrus waste, is estimated to total 15 million tons per year worldwide [5]. Although weight of the fruits and remain the primary byproduct [4]. This solid residue, referred to as citrus peels are used as cattle feed and as a source of essential oils, the correct management citrus waste, is estimated to total 15 million tons per year worldwide [5]. Although citrus of this residue remains an ongoing problem for the citrus industry [3]. The major compo- peels are used as cattle feed and as a source of essential oils, the correct management of nents of dry citrus peel waste include sugars (23%), cellulose (22%), pectin (25%), hemi- this residue remains an ongoing problem for the citrus industry [3]. The major components cellulose (11%), flavonoids (4.5%), and up to 4% essential oil, often referred to as citrus of dry citrus peel waste include sugars (23%), cellulose (22%), pectin (25%), hemicellulose essential oil [6]. (11%), flavonoids (4.5%), and up to 4% essential oil, often referred to as citrus essential oil [6]. 1.2. Production of Essential Oils 1.2. ProductionDifferent industries of Essential appreciate Oils citrus essential oils because of their pleasant aroma and incredibleDifferent industries variety of appreciate applications citrus [7]. essential In the food oils industry, because of citrus their pleasantessential aromaoil is used and incredibleas the main variety aromatic of applications ingredient in [7 ].non-alcoholic In the food industry, carbonated citrus drinks, essential cola oildrinks, is used pastries, as the mainsweets, aromatic and biscuits. ingredient In the in pharmaceutical non-alcoholic carbonated industry, this drinks, type cola of essential drinks, pastries, oil is used sweets, as a andflavoring biscuits. to mask In the the pharmaceutical unpleasant taste industry, of drugs this [8]. type In ofthe essential chemical oil industry, is usedas these a flavoring oils are toused mask as fragrances the unpleasant in air tastefresheners of drugs and [8 cleani]. In theng products. chemical industry,In the perfume these oilsindustry, are used citrus as fragrancesessential oils in airare freshenersused as the and primary cleaning raw products. materials In to the formulate perfume industry,toiletries citrusand perfumes essential oils[7]. are used as the primary raw materials to formulate toiletries and perfumes [7]. Citrus oil generally contains over 90% terpenes, about 5% oxygenated compounds, and less than than 1% 1% non-volatile non-volatile compounds, compounds, such such as as waxes waxes and and pigments pigments [9,10]. [9,10 ].Essential Essen- oilstial consist oils consist of mixtures of mixtures of volatile of volatile and non-volatile and non-volatile components, components, such as suchterpenes, as terpenes, sesquit- erpenes,sesquiterpenes, higher higheralcohols, alcohols, aldehydes, aldehydes, ketones, ketones, acids, esters, acids, esters,camphor, camphor, and waxes. and waxes. The volatilevolatile fractionfraction of of Persian Persian lime lime oil oil is characterizedis characterized by higherby higher levels levels of d-limonene, of d-limo- nene,γ-terpinene, γ-terpinene, esters, esters, and monoterpene and monoterpene aldehydes aldehydes and lower and amounts lower amounts of β-pinene of β +-pinene sabinene + sabinenesesquiterpenes sesquiterpenes and aliphatic and aliphatic aldehydes aldehydes than key than lime key oils lime [11 oils]. Interestingly, [11]. Interestingly, although alt- houghd-limonene d-limonene comprises comprises more than more 90% thanw/w 90%of the w/w volatile of the compositionvolatile composition of the essential of the essen- oil, its tialcontribution oil, its contribution to the final aromato the final of the aroma mixture of isthe limited mixture by itsis limited instability by andits instability the possibility and theof forming possibility off-flavor of forming compounds off-flavor [7]. compounds [7]. Some ofof thethe representative representative compounds compounds in thein essentialthe essential oil from oil Persianfrom Persian lime are lime shown are shownin Figure in1 Figure. 1. Figure 1. Compounds in in the the essential essential oil oil of of Persian Persian lime: lime: (a ()a d-limonene,) d-limonene, (b ()b γ)-terpinene,γ-terpinene, (c) (βc) -pinene,β -pinene, (d) (αd-terpineol,)
Recommended publications
  • Innovation in Continuous Rectification for Tequila Production

    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

    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

    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 ..................................................
  • Modelling of Crude Oil Distillation

    Modelling of Crude Oil Distillation

    Modelling of Crude Oil Distillation Modellering av råoljedestillation JENN Y BEATRIC E SOUC K K T H C h em i ca l S ci en c e and E n gi n e e r i n g Master’s Thesis in Chemical Engineering Stockholm, Sweden 2012 " One never notices what has been done; one can only see what remains to be done" (Marie Curie, 1867-1934) 1 Sammanfattning Under de föhållanden som reservoarens miljö erbjuder, definieras en petroleumvätska av dess termodynamiska och volymetriska egenskaper och av dess fysikalisk-kemiska egenskaper. För att korrekt simulera bearbetningen av dessa vätskor under produktion, deras beteende modelleras från experimentella data Med tillkomsten av nya regler och oflexibilitet som finns på tullbestämmelser vid gränserna idag, har forskningscenter stora svårigheter att få större mängder prover levererade. Av den anledningen, trots att det finns flera metoder för att karakterisera de olika komponenterna av råolja, tvingas laboratorier att vända sig mer och mer till alternativa analysmetoder som kräver mindre provvolymer: mikrodestillation, gaskromatografi, etc. Mikrodestillation, som är en snabb och helt datoriserad teknik, visar sig kunna ersätta standarddestillation för analys av flytande petroleumprodukter. Fördelar med metoden jämfört med standarddestillering är minskad arbetstidsåtgång med minst en faktor 4. Därtill krävs endast en [24] begränsad provvolym (några mikroliter) i jämförelse med standarddestillation. Denna rapport syftar till att skapa en enkel modell som kan förutsäga avkastningskurvan av fysisk destillation, utan att använda mikrodestillationsteknik. De resultat som erhölls genom gaskromatografiska analyser möjliggjorde modelleringen av det vätskebeteendet hos det analyserade provet. Efter att ha identifierat och behandlat praktiskt taget alla viktiga aspekter av mikro destillation genom simuleringar med PRO/II, fann jag att, oberoende av inställningen och den termodynamiska metod som används, det alltid finns stora skillnader mellan simulering och mikro destillation.
  • Review of Extractive Distillation. Process Design, Operation

    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.
  • Computer Simulation of a Multicomponent, Multistage Batch Distillation Process

    Computer Simulation of a Multicomponent, Multistage Batch Distillation Process

    COMPUTER SIMULATION OF A MULTICOMPONENT, MULTISTAGE BATCH DISTILLATION PROCESS By BRUCE EARL BAUGHER /J Bachelor of Science in Chemical Engineering Oklahoma State University Stillwater, Oklahoma 1985 Submitted to the Faculty of the Graduate College of the Oklahoma State University in partial fulfillment of the requirements for the Degree of MASTER OF SCIENCE July, 1988 \\,~s~ ~ \'\~~ B~~~to'­ <:.o?. ·;)._, ~ r COMPUTER SIMULATION OF A MULTICOMPONENT, MULTISTAGE BATCH DISTILLATION PROCESS Thesis Approved: Thesis Advisor U.bJ ~~- ~MJYl~ Dean of the GradU~te College ABSTRACT The material and energy balance equations for a batch distillation column were derived and a computer simulation was developed to solve these equations. The solution follows a modified Newton-Raphson approach for inverting and solving the matrices of material and energy balance equations. The model is unique in that it has been designed to handle hypothetical hydrocarbon components. The simulation can handle columns up to 50 trays and systems of up to 100 components. The model has been used to simulate True Boiling Point (TBP) diagrams for a variety of crude oils. This simulation is also applicable to simple laboratory batch distillations. The model was designed to accurately combine data files to simulate actual crude blending procedures. The model will combine files and calculate the results quickly and easily. The simulation involves removing material from the column at steady-state. The removal fraction is made small enough to approach continuity. This simulation can be adapted for use on microcomputers, although it will require extensive computation time. ACKNOWLEDGMENTS It has been a great pleasure to work with my thesis advisor, Dr.
  • Distillation Handbook

    Distillation Handbook

    I distillation terminology To provide a better understanding of the distillation process, the following briefly explains the terminology most often encountered. SOLVENT RECOVERY The term "solvent recovery" often has been a somewhat vague label applied to the many and very different ways in which solvents can be reclaimed by industry. One approach employed in the printing and coatings industries is merely to take impure solvents containing both soluble and insoluble particles and evapo- rate the solvent from the solids. For a duty of this type, APV offers the Paraflash evaporator, a compact unit which combines a Paraflow plate heat exchanger and a small separator. As the solvent ladened liquid is recirculated through the heat exchanger, it is evaporated and the vapor and liquid separated. This will recover a solvent but it will not separate solvents if two or more are present. Afurther technique is available to handle an air stream that carries solvents. By chilling the air by means of vent condensers or refrigeration equipment, the solvents can be removed from the condenser. Solvents also can be recovered by using extraction, adsorption, absorption, and distillation methods. S 0 LV E NT EXT R ACT I0 N Essentially a liquid/liquid process where one liquid is used to extract another from a secondary stream, solvent extraction generally is performed in a column somewhat similar to a normal distillation column. The primary difference is that the process involves two liquids instead of liquid and vapor. During the process, the lighter (i.e., less dense) liquid is charged to the base of the column and rises through packing or trays while the more dense liquid descends.
  • Hydro-Distillation and Steam Distillation from Aromatic Plants

    Hydro-Distillation and Steam Distillation from Aromatic Plants

    Hydro-distillation and steam distillation from aromatic plants Sudeep Tandon Scientist Chemical Engineering Division CIMAP, Lucknow HISTORY Written records of herbal distillation are found as early as the first century A.D., and around 1000 A.D., the noted Arab physician and naturalist Ibn Sina also known as Avicenna described the distillation of rose oil from rose petals The ancient Arabian people began to study the chemical properties of essential oils & developed and refined the distillation process Europeans began producing essential oils in the 12th century 1 DISTILLATION ? A process in which a liquid or vapour mixture of two or more substances is separated into its component fractions of desired purity, by the application and removal of heat. In simple terms distillation of aromatic herbs implies vaporizing or liberating the oils from the trichomes / plant cell membranes of the herb in presence of high temperature and moisture and then cooling the vapour mixture to separate out the oil from water. It is the most popular widely used and cost effective method in use today for producing majority of the essential oils throughout the world Distillation is an art and not just a “Chemical" process that is reliant upon many factors for successful quality oil production. BASIC SCIENTIFIC PRINCIPLES INVOLVED IN THE PROCESS To convert any liquid into a vapour we have to apply energy in form of heat called as latent heat of vaporization A liquid always boils at the temperature at which its vapour pressure equals the atmospheric / surrounding pressure For two immiscible liquids the total vapour pressure of the mixture is always equal to the sum of their partial pressures The composition of the mixture will be determined by the concentration of the individual components into its partial pressure As known the boiling point of most essential oil components exceeds that of water and generally lies between 150 – 300oC 2 If a sample of an essential oil having a component ‘A’ having boiling point for example 190oC and the boiling point of the water is 100oC.
  • Supercritical CO Extraction of Essential Oil from Clove

    Supercritical CO Extraction of Essential Oil from Clove

    Supercritical CO2 Extraction of Essential Oil from Clove Bud: Effect of Operation Conditions on the Selective Isolation of Eugenol and Eugenyl Acetate Farshad Yazdani, Morteza Mafi, Fathollah Farhadi, Kourosh Tabar-Heidar, Kioumars Aghapoor, Farshid Mohsenzadeh, and Hossein Reza Darabi Chemistry & Chemical Engineering Research Center of Iran, P.O. Box 14335-186, Teheran, Iran Reprint requests to Dr. H. R. Darabi. E-mail: [email protected] Z. Naturforsch. 60b, 1197 – 1201 (2005); received July 14, 2005 The supercritical fluid extraction (SFE) of clove bud essential oil was studied using CO2 as sol- vent. The effect of operation conditions was analyzed in a series of experiments at temperatures between 325 and 416 K and pressures between 110 and 190 bar. The collected extracts were ana- lyzed and the relative composition of the essential oil was determined. The optimum condition was found in a temperature of 353 K and at a pressure of 190 bar, minimizing the number of extracts to two compounds (eugenol and eugenyl acetate). The extract obtained from clove bud by using su- percritical fluid extraction was compared with the essential oil obtained by steam distillation and microwave-assisted extraction by considering both quantity and quality of the product. The oil yield was higher in steam distillation and microwave oven extraction. In contrast, oil extracted by using SFE contained higher amount of eugenol and eugenyl acetate. Key words: Clove Bud, Eugenol, Extraction Introduction The high pressure is used for processes where to- Identification, extraction and preparation of clove tal extraction of a target compound is desired, since bud oil are gaining interest as its applications are most extractable compounds exhibit their maximum becoming widespread in different sectors like food, solubility in a supercritical solvent at higher pressures.
  • Distillation ­ Accessscience from Mcgraw­Hill Education

    Distillation ­ Accessscience from Mcgraw­Hill Education

    6/19/2017 Distillation ­ AccessScience from McGraw­Hill Education (http://www.accessscience.com/) Distillation Article by: King, C. Judson University of California, Berkeley, California. Last updated: 2014 DOI: https://doi.org/10.1036/1097­8542.201100 (https://doi.org/10.1036/1097­8542.201100) Content Hide Simple distillations Fractional distillation Vapor­liquid equilibria Distillation pressure Molecular distillation Extractive and azeotropic distillation Enhancing energy efficiency Computational methods Stage efficiency Links to Primary Literature Additional Readings A method for separating homogeneous mixtures based upon equilibration of liquid and vapor phases. Substances that differ in volatility appear in different proportions in vapor and liquid phases at equilibrium with one another. Thus, vaporizing part of a volatile liquid produces vapor and liquid products that differ in composition. This outcome constitutes a separation among the components in the original liquid. Through appropriate configurations of repeated vapor­liquid contactings, the degree of separation among components differing in volatility can be increased manyfold. See also: Phase equilibrium (/content/phase­equilibrium/505500) Distillation is by far the most common method of separation in the petroleum, natural gas, and petrochemical industries. Its many applications in other industries include air fractionation, solvent recovery and recycling, separation of light isotopes such as hydrogen and deuterium, and production of alcoholic beverages, flavors, fatty acids, and food oils. Simple distillations The two most elementary forms of distillation are a continuous equilibrium distillation and a simple batch distillation (Fig. 1). http://www.accessscience.com/content/distillation/201100 1/10 6/19/2017 Distillation ­ AccessScience from McGraw­Hill Education Fig. 1 Simple distillations. (a) Continuous equilibrium distillation.
  • Building a Home Distillation Apparatus

    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

    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.