Separations: a Short History and a Cloudy Crystal Ball

Total Page:16

File Type:pdf, Size:1020Kb

Separations: a Short History and a Cloudy Crystal Ball ---11111111-•-----=--------~S=i AIChE special section ) SEPARATIONS: A SHORT HISTORY AND A CLOUDY CRYSTAL BALL PHIL WANKAT Purdue University eparations have always been and will continue to be still was invented by Jabir ibn Rayyan (aka Geber) in the late critically important in the processing of chemicals. 8th or early 9th century. Similar stills are currently in use in SIt is common to note that 40 to 70 % of both capital some whiskey distilleries and for distilling rose oil.[ 6l By the and operating costs in industry are due to separations_[!, P· lJ 14th century the production of strong alcoholic drinks had 4 18 It has been estimated that 15 % of the world's energy use become an industry. [ , P· l The first book on distillation was is required by separations.[2l Because of their industrial Hieronymus Brunschwig's Liber de arte distillandi published importance separations have always played an important in the early 1500s and translated into English in 1527_[7J part in chemical engineering education and in the chemical Brunschwig's book (Figure 1) is an apothecary with distilla­ engineering literature. tion used to produce various medicines from plants. Petroleum distillation was started in England in the 17th century and coal HISTORY OF SEPARATIONS tar distillation was first patented in 1746_[4, P· 35l Fractionation The beginning of separations apparently occurred before of coal tar into naphtha, kerosene, lubricating oil, and paraffin 3 recorded history. Egyptians used filtration to filter grape was patented in England in 1850. [ l The first oil refinery con­ 3 8990 juice over 5,000 years ago. [ , PP· l Aristotle mentioned that structed in 1860 in Pennsylvania used simple batch stills and 4 16 pure water can be obtained by evaporating sea water. [ , P· l A collected wide-boiling fractions as the distillation proceeded. combination of coagulation of impurities, evaporation, and crystallization used for salt manufacture were commonly in Phil Wankat has a joint appointment in 90 4 21 5 229 233 use by the 16th centuryY-P ' · PP ' · PP - l Similar practices Chemical Engineering and in Engineering 5 233 Education at Purdue University. He has a were still in use in India in 1980. [ , P· l Pressing, evaporation, B.S. ChE from Purdue, a Ph.D. from Princ­ and crystallization were commonly in use for sugar production eton, and an M.S. Ed from Purdue. He is by the 16th century.[4, P· 23 l the associate editor of GEE. Distillation, particularly batch distillation, has a long history. Mesopotamian clay distillation vessels with lids shaped to col­ lect the condensed volatile distillate have been dated to ~3500 BCE. [6l Alchemists in the first century AD in Alexandria used 4 16 a variety of simple batch stills or retorts_[ , P· l The alembic © Copyright ChE Division of ASEE 2009 286 Chemical Engineering Education ·_.~-/;;a~ ·. {J-ll/u£.,,,:: . ,..J}• ~o. ✓ •· 'L..~~ --P' - / ;;_/ <L ~ ' . 1.ibetr 'Oe aute iaiftil' htndi be CfompcfitfG. ·;z,as (!~cJ,-~et roaren kun,t 3u t>jJt~niaen t,i~ j ., rCtmpofita -on frmplaaa/~nb bl ~aidt t~cfaurue pattpcnv!-cnt f~at3 ~ ~trne gt~ ,w«)ica.riw~ie b»famliri rtef41.len w be bii~ertt ~ 2lr~li1 lt'11b bur~ ~~petitnefl ~ mil: J~eeonfmo b:iif~wicf ~ff gcclnbc ~ii ~e.offmbatt ~ii not'f ~enc bic e6 begcrc+ Figure 1. Cover page to Hieronymus Brunschwig's Liber de arte distillandi. Courtesy of Donald F. and Mildred Topp Othmer Library of Chemical History, Chemical Heritage Foundation, Philadelphia, PA. Vol. 43, No. 4, Fall 2009 287 1 257 Horizontal stills with improved performance were used in the Davis,l1 · P· l who notes that safety valves are useful if they are early 19th century for alcohol purification. An improved still kept in working order. Packing was apparently first employed was developed in 1818 by Cellier in France who developed in 1820 and was patented in 1847.[16l The problem of breaking 4 35 a vertical bubble plate still for alcohol purification_[ , P· l the ethanol water azeotrope was solved by Young in 1902 with In Victorian times large estates often had batch distillation a batch, azeotropic distillation process using benzene as the systems to prepare drugs and concentrated liquors. Popular entrainer to produce the first observed ternary azeotrope as books on distillation were available for this market. [9l In his the distillate product. The batch process was converted to a Handbook ofChemical Engineering, published in 1901 and in continuous azeotropic distillation by Keyes in 1928Y7l an enlarged edition in 1904, George Davis clearly developed In the early 1920s petroleum refineries had not adopted 0 the unit operations idea (not by this name) for distillationY · more modem fractionation systems and were using horizon­ 100 103 11 PP· - , l Before this, the distillation of each chemical was tal stills directly heated on the bottom in conjunction with studied separately. It is notable that the 2nd edition of C. partial condensation to distil petroleum. These systems were 12 S. Robinson's The Elements of Fractional Distillation[ i not very efficient and considerable redistilling was required. has elements of both the unit operations generalization and Modernization of distillation in refineries occurred in the individual chapters for distillation of a number of chemicals 1920s when W.K. Lewis was hired as a consultant by the such as ethanol. By the fourth edition, extensively revised by Standard Oil Company of New Jersey and introduced vertical 3 Ed Gilliland,l1 l the unit operations approach dominated and 8 305306 fractionation systems.[ , PP· l By the 1920s and 1930s the distillation of specific chemicals were relegated to examples. 12 18 schematics of continuous distillation columns in textbooks[ ' ' 19 20 12 The Elements of Fractional Distillation may have been the l and in Perry's HandbooAf. · section i look fairly modem except first chemical engineering book to also become popular with a that valve trays and structured packings had not been invented nontechnical audience-it was very popular with bootleggers yet. Heat recovery in distillation was common by 1923Y-P 575l 14 85 in the 1920s and 1930s.[ ,p. l Batch distillation was important The histories of distillation equipment, distillation control, enough to attract the attention of Lord Rayleigh who appar­ and azeotropic and extractive distillation were reviewed by 5 ently did the first theoretical analysis of the methodY l Fair,l1 6l Buckley,l2 1l and Othmer,l1 7l respectively, for the 75th The first continuous distillation appears to have been de­ anniversary of AIChE. veloped by Aeneas Coffey in 1830. He developed a vertical Theoretical analysis of continuous binary distillation was 4 perforated plate column for alcohol purification (Figure 2). [ , PP· first achieved by Sorel, who was interested in the distillation 35 36 11 ' l This still was equipped to preheat the feed by exchange of alcoholP2l Sorel's method is accurate, but confusing and with the condensing distillate and the bottoms. Davis[lll shows laborious since a trial-and-error calculation was required on open-steam distillation systems and several examples of every stage. Binary distillation was analyzed graphically with­ methods to reduce energy. In 1900 vertical perforated plate out trial-and-error by Ponchon[23 J and Savarit[24l independently. columns quite similar to modem equipment were introduced Lewis[25J realized that in many cases the vapor and liquid molar 4 36 9 for distillation of tar. [ , P· ' al Safety in tar stills is discussed by flow rates are approximately constant-if they are assumed to Figure 2. "The Coffey still of 1830 for distilling alco­ hol from fermented mash, using perforated plates. 1. Boiler. 3. Stripping col­ umn. 4. Rectifying column. 6. Feed. 8. Condenser. " Reprinted with permission from Davies, J. T., "Chemi­ cal Engineering: How Did it Begin and Develop?" in Furter, WF. (Ed.), History of Chemical Engineering, American Chemical Soci­ ety, Washington, D.C., Ad- vances in Chemistry Series, 190, 15-43 (1980). Copyright 1980 American Chemical Society. 288 Chemical Engineering Education be constant Sorel's trial-and-error procedure is not required. Gibbs studied the thermodynamics of growing crystal surfaces The simplified Lewis method was converted to a graphical at equilibrium and realized that thermodynamics was often method by McCabe and Thiele. [26l Because McCabe-Thiele not sufficient to explain the crystal growth.[36l McCabe[37l plots clarified the physical reasons why column distillation found that the deposition rate/unit area is often linear in works, the method was rapidly adopted. While no longer used supersaturation and deposits grow at a uniform rate. Unfor­ for design, McCabe-Thiele diagrams are commonly used to tunately, McCabe's L law often does not holdY6l Industrial teach distillation. Solutions for multicomponent distillation scale crystallizers in 1934[33l do not look very different than are much more complicated, particularly if there are non-dis­ many modem crystallizers. The important theory of crystal tributing light and heavy non-keys. Initially, stage-by-stage size distribution was developed by Randolph and LarsonY9l 7 28 36 methods were adapted to multicomponent distillation,(2 ' l Hulbert[ l reviewed crystallization for the 75th anniversary but closure remained a problem. Numerous computer solution of AIChE, and more recent advances in crystal engineering methods were developed after Amundson and Pontinen[29J are reviewed by Doherty. [4oJ Precipitation is similar to crystal­ realized that distillation equations could be conveniently lization except the product is usually amorphous with a poorly solved after they were put into matrix form. One of the more defined shape and structure. Precipitation is often used as a robust and common methods still used in commercial simula­ first cut before crystallization. Early workers did not delineate tors was Naphtali and Sandholm's[30] linearization of all the between precipitation and crystallization and many early equations.
Recommended publications
  • 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.
    [Show full text]
  • Gas Chromatography-Mass Spectroscopy
    Gas Chromatography-Mass Spectroscopy Introduction Gas chromatography-mass spectroscopy (GC-MS) is one of the so-called hyphenated analytical techniques. As the name implies, it is actually two techniques that are combined to form a single method of analyzing mixtures of chemicals. Gas chromatography separates the components of a mixture and mass spectroscopy characterizes each of the components individually. By combining the two techniques, an analytical chemist can both qualitatively and quantitatively evaluate a solution containing a number of chemicals. Gas Chromatography In general, chromatography is used to separate mixtures of chemicals into individual components. Once isolated, the components can be evaluated individually. In all chromatography, separation occurs when the sample mixture is introduced (injected) into a mobile phase. In liquid chromatography (LC), the mobile phase is a solvent. In gas chromatography (GC), the mobile phase is an inert gas such as helium. The mobile phase carries the sample mixture through what is referred to as a stationary phase. The stationary phase is usually a chemical that can selectively attract components in a sample mixture. The stationary phase is usually contained in a tube of some sort called a column. Columns can be glass or stainless steel of various dimensions. The mixture of compounds in the mobile phase interacts with the stationary phase. Each compound in the mixture interacts at a different rate. Those that interact the fastest will exit (elute from) the column first. Those that interact slowest will exit the column last. By changing characteristics of the mobile phase and the stationary phase, different mixtures of chemicals can be separated.
    [Show full text]
  • Qualitative and Quantitative Analysis
    qualitative and quantitative analysis Russian scientist Tswett in 1906 used a glass columns packed with divided CaCO3(calcium carbonate) to separate plant pigments extracted by hexane. The pigments after separation appeared as colour bands that can come out of the column one by one. Tswett was the first to use the term "chromatography" derived from two Greek words "Chroma" meaning color and "graphein" meaning to write. Invention of Chromatography by M. Tswett Ether Chromatography Colors Chlorophyll CaCO3 5 *Definition of chromatography *Tswett (1906) stated that „chromatography is a method in which the components of a mixture are separated on adsorbent column in a flowing system”. *IUPAC definition (International Union of pure and applied Chemistry) (1993): Chromatography is a physical method of separation in which the components to be separated are distributed between two phases, one of which is stationary while the other moves in a definite direction. *Principles of Chromatography * Any chromatography system is composed of three components : * Stationary phase * Mobile phase * Mixture to be separated The separation process occurs because the components of mixture have different affinities for the two phases and thus move through the system at different rates. A component with a high affinity for the mobile phase moves quickly through the chromatographic system, whereas one with high affinity for the solid phase moves more slowly. *Forces Responsible for Separation * The affinity differences of the components for the stationary or the mobile phases can be due to several different chemical or physical properties including: * Ionization state * Polarity and polarizability * Hydrogen bonding / van der Waals’ forces * Hydrophobicity * Hydrophilicity * The rate at which a sample moves is determined by how much time it spends in the mobile phase.
    [Show full text]
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • Distillation Theory
    Chapter 2 Distillation Theory by Ivar J. Halvorsen and Sigurd Skogestad Norwegian University of Science and Technology Department of Chemical Engineering 7491 Trondheim, Norway This is a revised version of an article published in the Encyclopedia of Separation Science by Aca- demic Press Ltd. (2000). The article gives some of the basics of distillation theory and its purpose is to provide basic understanding and some tools for simple hand calculations of distillation col- umns. The methods presented here can be used to obtain simple estimates and to check more rigorous computations. NTNU Dr. ing. Thesis 2001:43 Ivar J. Halvorsen 28 2.1 Introduction Distillation is a very old separation technology for separating liquid mixtures that can be traced back to the chemists in Alexandria in the first century A.D. Today distillation is the most important industrial separation technology. It is particu- larly well suited for high purity separations since any degree of separation can be obtained with a fixed energy consumption by increasing the number of equilib- rium stages. To describe the degree of separation between two components in a column or in a column section, we introduce the separation factor: ()⁄ xL xH S = ------------------------T (2.1) ()x ⁄ x L H B where x denotes mole fraction of a component, subscript L denotes light compo- nent, H heavy component, T denotes the top of the section, and B the bottom. It is relatively straightforward to derive models of distillation columns based on almost any degree of detail, and also to use such models to simulate the behaviour on a computer.
    [Show full text]
  • Laser Desorption/Ionization Time-Of-Flight Mass Spectrometry of Biomolecules Yu-Chen Chang Iowa State University
    Iowa State University Capstones, Theses and Retrospective Theses and Dissertations Dissertations 1996 Laser desorption/ionization time-of-flight mass spectrometry of biomolecules Yu-chen Chang Iowa State University Follow this and additional works at: https://lib.dr.iastate.edu/rtd Part of the Analytical Chemistry Commons Recommended Citation Chang, Yu-chen, "Laser desorption/ionization time-of-flight mass spectrometry of biomolecules " (1996). Retrospective Theses and Dissertations. 11366. https://lib.dr.iastate.edu/rtd/11366 This Dissertation is brought to you for free and open access by the Iowa State University Capstones, Theses and Dissertations at Iowa State University Digital Repository. It has been accepted for inclusion in Retrospective Theses and Dissertations by an authorized administrator of Iowa State University Digital Repository. For more information, please contact [email protected]. INFORMATION TO USERS This manuscript has been rqjroduced fix>m the microfihn master. UMI fihns the text directly from the original or copy submitted. Thus, some thesis and dissertation copies are in typewriter face, w^e others may be from any type of computer printer. The quality of this reproduction is dependent upon the quality of the copy submitted. Broken or indistinct print, colored or poor quality illustrations and photographs, print bleedthrough, substandard margins, and improper alignment can adversely afifect reproduction. In the unlikely event that the author did not send IMl a complete manuscript and there are misang pages, these will be noted. Also, if unauthorized copyright material had to be removed, a note will indicate the deletion. Oversize materials (e.g., maps, drawings, charts) are reproduced by sectioning the original, beginning at the upper left-hand comer and continuing from left to right in equal sections with small overlaps.
    [Show full text]
  • Separations Development and Application (WBS 2.4.1.101) U.S
    Separations Development and Application (WBS 2.4.1.101) U.S. Department of Energy (DOE) Bioenergy Technologies Office (BETO) 2017 Project Peer Review James D. (“Jim”) McMillan NREL March 7, 2017 Biochemical Conversion Session This presentation does not contain any proprietary, confidential, or otherwise restricted information. Project Goal Overall goal: Define, develop and apply separation processes to enable cost- effective hydrocarbon fuel / precursor production; focus on sugars and fuel precursor streams; lipids pathway shown. Outcome: Down selected proven, viable methods for clarifying and concentrating the sugar intermediates stream and for recovering lipids from oleaginous yeast that pass “go” criteria (i.e., high yield, scalable, and cost effective). Relevance: Separations are key to overall process integration and economics; often represent ≥ 50% of total process costs; performance/efficiency can make or break process viability. Separations this project investigates – sugar stream clarification and concentration, and recovery of intracellular lipids from yeast – account for 17-26% of projected Minimum Fuel Selling Price (MFSP) for the integrated process. 2 Project Overview • Cost driven R&D to assess/develop/improve key process separations - Sugar stream separations: S/L, concentrative and polishing - Fuel precursor recovery separations: oleaginous yeast cell lysis and LLE lipid recovery • Identify and characterize effective methods - Show capability to pass relevant go/no-go criteria (e.g., high yield, low cost, scalable) • Exploit in situ separation for process intensification - Enable Continuous Enzymatic Hydrolysis (CEH) • Generate performance data to develop / refine process TEAs and LCAs 3 Separations Technoeconomic Impact $1.78 $2.18 $1.43 $0.79 4 Quad Chart Overview Timeline Barriers Primary focus on addressing upstream and Start: FY 15 (Oct., ‘14) downstream separations-related barriers: End: FY 17 (Sept., ‘17; projected) – Ct-G.
    [Show full text]
  • Rubber-Modified Epoxies: in Situ Detection of the Phase Separation by Differential Scanning Calorimetry
    Rubber-modified epoxies: in situ detection of the phase separation by differential scanning calorimetry Dong Pu Fang*, C. C. Riccardi and R. J. J. Williamst Institute of Materials Science and Technology (INTEMA), University of Mar de/Plata and National Research Council (CONICET), J. B. Justo 4302, 7600 Mar de/Plata, Argentina (Received 18 May 1993) The phase separation of a rubber in the course of a thermosetting polymerization is associated with heat release. Mixing is endothermic as revealed by the positive value of the interaction parameter while demixing is exothermic. Differential scanning calorimetry may be used to detect heat effects related to phase separation. Experimental results are reported for an unreactive system (castor oil/epoxy resin) and reactive systems (modifier/epoxy resin/diamine) using either castor oil or epoxy-terminated copolymers of acrylonitrile and butadiene as modifiers. (Keywords: rubber-modified epoxies; phase separation; d.s.c.) Introduction represents the residual free energy of mixing (part or all A common method to toughen epoxy resins is to of it may be considered as an enthalpic contribution). dissolve rubbers or other modifiers that become phase- The interaction parameter A, expressed in units of energy separated in the course of polymerization. The resulting per unit volume, is usually a positive value. This means two-phase structure exhibits an increase in the fracture that mixing occurs due to the prevailing influence of the resistance at the expense of lower values of the elastic combinatorial part of the equation over the interaction modulus and yield stress. term. Dissimilar molecules (positive A) are thus obliged Monitoring the phase separation process is important to mix due to an entropic driving force; their intrinsic in two respects: (i) for unreactive epoxy-rubber repulsion is manifested by an endothermic effect in the formulations, i.e.
    [Show full text]
  • 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.
    [Show full text]
  • Advanced Separation Techniques Combined with Mass Spectrometry for Difficult Analytical Tasks - Isomer Separation and Oil Analysis
    FINNISH METEOROLOGICAL INSTITUTE Erik Palménin aukio 1 P.O. Box 503 FI-00101 HELSINKI 131 CONTRIBUTIONS tel. +358 29 539 1000 WWW.FMI.FI FINNISH METEOROLOGICAL INSTITUTE CONTRIBUTIONS No. 131 ISBN 978-952-336-016-7 (paperback) ISSN 0782-6117 Erweko Helsinki 2017 ISBN 978-952-336-017-4 (pdf) Helsinki 2017 ADVANCED SEPARATION TECHNIQUES COMBINED WITH MASS SPECTROMETRY FOR DIFFICULT ANALYTICAL TASKS - ISOMER SEPARATION AND OIL ANALYSIS JAAKKO LAAKIA Department of Chemistry University of Helsinki Finland Advanced separation techniques combined with mass spectrometry for difficult analytical tasks – isomer separation and oil analysis Jaakko Laakia Academic Dissertation To be presented, with the permission of the Faculty of Science of the University of Helsinki, for public criticism in Auditorium A129 of the Department of Chemistry (A.I. Virtasen aukio 1, Helsinki) on May 12th, 2017, at 12 o’clock noon. Helsinki 2017 1 TABLE OF CONTENTS ABSTRACT 4 Supervisors Professor Tapio Kotiaho TIIVISTELMÄ 5 Department of Chemistry LIST OF ORIGINAL PAPERS 6 Faculty of Science ACKNOWLEDGEMENTS 7 ABBREVIATIONS 8 and 1. INTRODUCTION 10 Division of Pharmaceutical Chemistry and Technology 1.1.1 Basic operation principles of ion mobility 12 spectrometry 11 Faculty of Pharmacy 1.1.2 Applications of ion mobility spectrometry 16 University of Helsinki 1.2 Basic operation principles and applications of two-dimensional gas 19 chromatography – time-of-flight mass spectrometry Docent Tiina Kauppila 1.3 Aims of study 23 Division of Pharmaceutical Chemistry and Technology
    [Show full text]
  • Comparison of Complete Extractive and Azeotropic Distillation Processes for Anhydrous Ethanol Production Using Aspen Plustm Simu
    43 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 80, 2020 The Italian Association of Chemical Engineering Online at www.cetjournal.it Guest Editors: Eliseo Maria Ranzi, Rubens Maciel Filho Copyright © 2020, AIDIC Servizi S.r.l. DOI: 10.3303/CET2080008 ISBN 978-88-95608-78-5; ISSN 2283-9216 Comparison of Complete Extractive and Azeotropic Distillation Processes for Anhydrous Ethanol Production using Aspen PlusTM Simulator Nahieh T. Miranda*, Rubens Maciel Filho, Maria Regina Wolf Maciel Laboratory of Optimization, Design, and Advanced Control (LOPCA)/Laboratory of Development of Separation Processes (LDPS), School of Chemical Engineering, University of Campinas, Brazil. [email protected] Performance of the extractive and azeotropic distillation processes using ethylene glycol and cyclohexane as solvents, respectively, for anhydrous ethanol production, were investigated using 02 RadFrac columns each and solvent recycling streams via simulation in Aspen Plus™ Simulator. Both operate at 1 atm, and feed flow -1 rate equals to 100 kmol.h (ethanol – 0.896 and water – 0.104 in mole fractions at the azeotropic point). The NRTL-RK was the model used for extractive and azeotropic distillations. The anhydrous ethanol purity from top of the 1st column of the extractive distillation (22 stages) was 99.50 % (on a mole basis) and water with nd st 99.20 % of purity at the top of the 2 column. On the other hand, in the azeotropic distillation, the 1 column (30 stages) had a bottom product of anhydrous ethanol purity of 99.99 % and water with 99.99 % of purity in the 2nd column, also at the bottom. Both processes produced anhydrous ethanol with a high-grade purity required by the standard norms ASTM D4806, EN 15376, and ANP 36.
    [Show full text]