Separations: a Short History and a Cloudy Crystal Ball
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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. -
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. -
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. -
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. -
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. -
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. -
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. -
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. -
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. -
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. -
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 -
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.