The Halothane/Ether Azeotrope - a Reconsideration
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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. -
Development of a Process for N-Butanol Recovery from Abe
937 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 74, 2019 The Italian Association of Chemical Engineering Online at www.cetjournal.it Guest Editors: Sauro Pierucci, Jiří Jaromír Klemeš, Laura Piazza Copyright © 2019, AIDIC Servizi S.r.l. ISBN 978-88-95608-71-6; ISSN 2283-9216 DOI: 10.3303/CET1974157 Development of a Process for N-Butanol Recovery from Abe Wastewater Streams by Membrane Technology * Marco Stoller , Marco Bravi, Paola Russo, Roberto Bubbico, Barbara Mazzarotta Sapienza University of Rome, Dept. of Chemical Materials Environmental Engineering, Via Eudossiana 18, 00184 Rome, Italy [email protected] The aceton-butyl-ethanolic fermentation process (ABE) is a biotechnological process that leads to the production of acetone, n-butanol and ethanol (ABE compounds) from glucose sources and amides by use of certain biomasses. The process was developed initially during the middle of the last century and suffers from decline due to the greater petrochemical production of products and the lowering of the costs of the sector. Nowadays, the ABE process is regaining great interest because the fraction with the highest concentration, i.e. n-butanol, is an excellent constituent for biofuels. The ABE process has been optimized over time to obtain maximum yields of n-butanol, but the problem of separating and concentrating the butanol in the outlet stream of the ABE process persists. To allow an adequate use, often distillation by use of more columns is required. Moreover, the contained biomasses and suspended solids, in high quantity, must be eliminated, leading to overall high treatment costs. This work will report the main idea and some preliminary experimental results for the development and application of a process based on membrane technologies, to separate and concentrate the butanol from ABE process streams to sensibly reduce the difficulty to perform a final distillation. -
Evaluation of Azeotropic Dehydration for the Preservation of Shrimp. James Edward Rutledge Louisiana State University and Agricultural & Mechanical College
Louisiana State University LSU Digital Commons LSU Historical Dissertations and Theses Graduate School 1969 Evaluation of Azeotropic Dehydration for the Preservation of Shrimp. James Edward Rutledge Louisiana State University and Agricultural & Mechanical College Follow this and additional works at: https://digitalcommons.lsu.edu/gradschool_disstheses Recommended Citation Rutledge, James Edward, "Evaluation of Azeotropic Dehydration for the Preservation of Shrimp." (1969). LSU Historical Dissertations and Theses. 1689. https://digitalcommons.lsu.edu/gradschool_disstheses/1689 This Dissertation is brought to you for free and open access by the Graduate School at LSU Digital Commons. It has been accepted for inclusion in LSU Historical Dissertations and Theses by an authorized administrator of LSU Digital Commons. For more information, please contact [email protected]. This dissertation has been 70-9089 microfilmed exactly as received RUTLEDGE, James Edward, 1941- EVALUATION OF AZEOTROPIC DEHYDRATION FOR THE PRESERVATION OF SHRIMP. The Louisiana State University and Agricultural and Mechanical College, PhJD., 1969 Food Technology University Microfilms, Inc., Ann Arbor, Michigan Evaluation of Azeotropic Dehydration for the Preservation of Shrimp A Dissertation Submitted to the Graduate Faculty of the Louisiana State University and Agricultural and Mechanical College in partial fulfillment of the requirements for the degree of Doctor of Philosophy in The Department of Food Science and Technology by James Edward Rutledge B.S., Texas A&M University, 1963 M.S., Texas A&M University, 1966 August, 1969 ACKNOWLEDGMENT The author wishes to express his sincere appreciation to his major professor, Dr, Fred H. Hoskins, for the guidance which he supplied not only in respect to this dissertation but also in regard to the author’s graduate career at Louisiana State University, Gratitude is also extended to Dr. -
Management of Chronic Problems
MANAGEMENT OF CHRONIC PROBLEMS INTERACTIONS BETWEEN ALCOHOL AND DRUGS A. Leary,* T. MacDonald† SUMMARY concerned. Alcohol may alter the effects of the drug; drug In western society alcohol consumption is common as is may change the effects of alcohol; or both may occur. the use of therapeutic drugs. It is not surprising therefore The interaction between alcohol and drug may be that concomitant use of these should occur frequently. The pharmacokinetic, with altered absorption, metabolism or consequences of this combination vary with the dose of elimination of the drug, alcohol or both.2 Alcohol may drug, the amount of alcohol taken, the mode of affect drug pharmacokinetics by altering gastric emptying administration and the pharmacological effects of the drug or liver metabolism. Drugs may affect alcohol kinetics by concerned. Interactions may be pharmacokinetic or altering gastric emptying or inhibiting gastric alcohol pharmacodynamic, and while coincidental use of alcohol dehydrogenase (ADH).3 This may lead to altered tissue may affect the metabolism or action of a drug, a drug may concentrations of one or both agents, with resultant toxicity. equally affect the metabolism or action of alcohol. Alcohol- The results of concomitant use may also be principally drug interactions may differ with acute and chronic alcohol pharmacodynamic, with combined alcohol and drug effects ingestion, particularly where toxicity is due to a metabolite occurring at the receptor level without important changes rather than the parent drug. There is both inter- and intra- in plasma concentration of either. Some interactions have individual variation in the response to concomitant drug both kinetic and dynamic components and, where this is and alcohol use. -
FUGACITY It Is Simply a Measure of Molar Gibbs Energy of a Real Gas
FUGACITY It is simply a measure of molar Gibbs energy of a real gas . Modifying the simple equation for the chemical potential of an ideal gas by introducing the concept of a fugacity (f). The fugacity is an “ effective pressure” which forces the equation below to be true for real gases: θθθ f µµµ ,p( T) === µµµ (T) +++ RT ln where pθ = 1 atm pθθθ A plot of the chemical potential for an ideal and real gas is shown as a function of the pressure at constant temperature. The fugacity has the units of pressure. As the pressure approaches zero, the real gas approach the ideal gas behavior and f approaches the pressure. 1 If fugacity is an “effective pressure” i.e, the pressure that gives the right value for the chemical potential of a real gas. So, the only way we can get a value for it and hence for µµµ is from the gas pressure. Thus we must find the relation between the effective pressure f and the measured pressure p. let f = φ p φ is defined as the fugacity coefficient. φφφ is the “fudge factor” that modifies the actual measured pressure to give the true chemical potential of the real gas. By introducing φ we have just put off finding f directly. Thus, now we have to find φ. Substituting for φφφ in the above equation gives: p µ=µ+(p,T)θ (T) RT ln + RT ln φ=µ (ideal gas) + RT ln φ pθ µµµ(p,T) −−− µµµ(ideal gas ) === RT ln φφφ This equation shows that the difference in chemical potential between the real and ideal gas lies in the term RT ln φφφ.φ This is the term due to molecular interaction effects. -
Euthanasia of Experimental Animals
EUTHANASIA OF EXPERIMENTAL ANIMALS • *• • • • • • • *•* EUROPEAN 1COMMISSIO N This document has been prepared for use within the Commission. It does not necessarily represent the Commission's official position. A great deal of additional information on the European Union is available on the Internet. It can be accessed through the Europa server (http://europa.eu.int) Cataloguing data can be found at the end of this publication Luxembourg: Office for Official Publications of the European Communities, 1997 ISBN 92-827-9694-9 © European Communities, 1997 Reproduction is authorized, except for commercial purposes, provided the source is acknowledged Printed in Belgium European Commission EUTHANASIA OF EXPERIMENTAL ANIMALS Document EUTHANASIA OF EXPERIMENTAL ANIMALS Report prepared for the European Commission by Mrs Bryony Close Dr Keith Banister Dr Vera Baumans Dr Eva-Maria Bernoth Dr Niall Bromage Dr John Bunyan Professor Dr Wolff Erhardt Professor Paul Flecknell Dr Neville Gregory Professor Dr Hansjoachim Hackbarth Professor David Morton Mr Clifford Warwick EUTHANASIA OF EXPERIMENTAL ANIMALS CONTENTS Page Preface 1 Acknowledgements 2 1. Introduction 3 1.1 Objectives of euthanasia 3 1.2 Definition of terms 3 1.3 Signs of pain and distress 4 1.4 Recognition and confirmation of death 5 1.5 Personnel and training 5 1.6 Handling and restraint 6 1.7 Equipment 6 1.8 Carcass and waste disposal 6 2. General comments on methods of euthanasia 7 2.1 Acceptable methods of euthanasia 7 2.2 Methods acceptable for unconscious animals 15 2.3 Methods that are not acceptable for euthanasia 16 3. Methods of euthanasia for each species group 21 3.1 Fish 21 3.2 Amphibians 27 3.3 Reptiles 31 3.4 Birds 35 3.5 Rodents 41 3.6 Rabbits 47 3.7 Carnivores - dogs, cats, ferrets 53 3.8 Large mammals - pigs, sheep, goats, cattle, horses 57 3.9 Non-human primates 61 3.10 Other animals not commonly used for experiments 62 4. -
Pharmacology – Inhalant Anesthetics
Pharmacology- Inhalant Anesthetics Lyon Lee DVM PhD DACVA Introduction • Maintenance of general anesthesia is primarily carried out using inhalation anesthetics, although intravenous anesthetics may be used for short procedures. • Inhalation anesthetics provide quicker changes of anesthetic depth than injectable anesthetics, and reversal of central nervous depression is more readily achieved, explaining for its popularity in prolonged anesthesia (less risk of overdosing, less accumulation and quicker recovery) (see table 1) Table 1. Comparison of inhalant and injectable anesthetics Inhalant Technique Injectable Technique Expensive Equipment Cheap (needles, syringes) Patent Airway and high O2 Not necessarily Better control of anesthetic depth Once given, suffer the consequences Ease of elimination (ventilation) Only through metabolism & Excretion Pollution No • Commonly administered inhalant anesthetics include volatile liquids such as isoflurane, halothane, sevoflurane and desflurane, and inorganic gas, nitrous oxide (N2O). Except N2O, these volatile anesthetics are chemically ‘halogenated hydrocarbons’ and all are closely related. • Physical characteristics of volatile anesthetics govern their clinical effects and practicality associated with their use. Table 2. Physical characteristics of some volatile anesthetic agents. (MAC is for man) Name partition coefficient. boiling point MAC % blood /gas oil/gas (deg=C) Nitrous oxide 0.47 1.4 -89 105 Cyclopropane 0.55 11.5 -34 9.2 Halothane 2.4 220 50.2 0.75 Methoxyflurane 11.0 950 104.7 0.2 Enflurane 1.9 98 56.5 1.68 Isoflurane 1.4 97 48.5 1.15 Sevoflurane 0.6 53 58.5 2.5 Desflurane 0.42 18.7 25 5.72 Diethyl ether 12 65 34.6 1.92 Chloroform 8 400 61.2 0.77 Trichloroethylene 9 714 86.7 0.23 • The volatile anesthetics are administered as vapors after their evaporization in devices known as vaporizers. -
By a 965% ATT'ys
July 19, 1960 A. WATZL ETAL 2,945,788 PROCESS FOR THE PURIFICATION OF DIMETHYLTEREPHTHALATE Filed Nov. 19, l956 AZEOTROPE DISTILLATE CONDENSER CONDENSED WACUUM DISTILLATE DRY DISTILLATION MXTURE N2 COLUMN MPURE - SOD WACUUMFILTER ETHYLENE DMETHYL DMETHYL GLYCOL TEREPHTHALATE TEREPHTHALATE ETHYLENE GLYCOL INVENTORS: ANTON WATZL by aERHARD 965% SIGGEL ATT'YS 2,945,788 Patented July 19, 1960 2 phthalate is immediately suitable for reesterification or Subsequent polycondensation to polyethylene terephthal 2,945,788 ate. There are gained polycondensates of high degree of PROCESS FOR THE PURIFICATION OF viscosity with K values from 50 to 57. DMETHYLTEREPHTHALATE The best mode contemplated for practicing the inven Anton Watz, Kleinwallstadt (Ufr), and Erhard Siggel, tion involves the use of ethylene glycol as the aliphatic Laudenbach (Main), Germany, assignors to Vereinigte glycol. The following is a specific illustration thereof. Glanzstoff-Fabriken A.G., Wuppertal-Elberfeld, Ger Example many Thirty grams of crude dimethylterephthalate are mixed Filed Nov.19, 1956, Ser. No. 622,778 in a flask with 270 grams of ethylene glycol and azeo tropically distilled with the introduction of dry nitrogen 4 Claims. (C. 202-42) in a column of 30 cm. at about 44 Torr (1 Torr equals 1 mm. Hg). The azeotrope goes over at about 120° C. i This invention, in general, relates to production of into a cooled condenser. The dimethylterephthalate dimethylterephthalate and more particularly to the puri 5 separated from the glycol by vacuum filtering can be fication thereof. used immediately for reesterification or for polyconden The purification of dimethylterephthalate can be car sation. This process is illustrated in the flow sheet of ried out either by distillation or by recrystallization from the accompanying drawing. -
Heterogeneous Azeotropic Distillation
PROSIMPLUS APPLICATION EXAMPLE HETEROGENEOUS AZEOTROPIC DISTILLATION EXAMPLE PURPOSE This example illustrates a high purity separation process of an azeotropic mixture (ethanol-water) through heterogeneous azeotropic distillation. This process includes distillation columns. Additionally these rigorous multi- stage separation modules are part of a recycling stream, demonstrating the efficiency of ProSimPlus convergence methods. Specifications are set on output streams in order to insure the required purity. This example illustrates the way to set "non-standard" specifications in the multi-stage separation modules. Three phase calculations (vapor-liquid- liquid) are done with the taken into account of possible liquid phase splitting. ACCESS Free-Internet Restricted to ProSim clients Restricted Confidential CORRESPONDING PROSIMPLUS FILE PSPS_EX_EN-Heterogeneous-Azeotropic-Distillation.pmp3 . Reader is reminded that this use case is only an example and should not be used for other purposes. Although this example is based on actual case it may not be considered as typical nor are the data used always the most accurate available. ProSim shall have no responsibility or liability for damages arising out of or related to the use of the results of calculations based on this example. Copyright © 2009 ProSim, Labège, France - All rights reserved www.prosim.net Heterogeneous azeotropic distillation Version: March, 2009 Page: 2 / 12 TABLE OF CONTENTS 1. PROCESS MODELING 3 1.1. Process description 3 1.2. Process flowsheet 5 1.3. Specifications 6 1.4. Components 6 1.5. Thermodynamic model 7 1.6. Operating conditions 7 1.7. "Hints and Tips" 9 2. RESULTS 9 2.1. Comments on results 9 2.2. Mass and energy balances 10 2.3. -
Diluted Isoflurane As a Suitable Alternative for Diethyl Ether for Rat Anaesthesia in Regular Toxicology Studies
FULL PAPER Laboratory Aminal Science Diluted Isoflurane as a Suitable Alternative for Diethyl ether for Rat Anaesthesia in Regular Toxicology Studies Toshiaki NAGATE1)*, Tomonobu CHINO1), Chizuru NISHIYAMA1), Daisuke OKUHARA1), Toru TAHARA1), Yoshimasa MARUYAMA1), Hiroko KASAHARA1), Kayoko TAKASHIMA1), Sayaka KOBAYASHI1), Yoshiyuki MOTOKAWA1), Shin-ichi MUTO1) and Junji KURODA1) 1)Toxicology Research Laboratory, R&D, Kissei Pharmaceutical Co., Ltd., 2320–1 Maki, Hotaka, Azumino-City, Nagano-Pref. 399–8305, Japan (Received 6 October 2006/Accepted 20 July 2007) ABSTRACT. Despite its explosive properties and toxicity to both animals and humans, diethyl ether is an agent long used in Japan in the anaesthesia jar method of rat anaesthetises. However, in response to a recent report from the Science Council of Japan condemning diethyl ether as acceptable practice, we searched for an alternative rat anaesthesia method that provided data continuous with pre-existing regular toxicology studies already conducted under diethyl ether anaesthesia. For this, we examined two candidates; 30% isoflurane diluted with propylene glycol and pentobarbitone. Whereas isoflurane is considered to be one of the representatives of modern volatile anaesthetics, the method of propylene glycol-diluted 30% isoflurane used in this study was our modification of a recently reported method revealed to have several advantages as an inhalation anaesthesia. Intraperitoneal pentobarbitone has long been accepted as a humane method in laboratory animal anaesthesiology. These 2 modalities were scrutinized in terms of consistency of haematology and blood chemistry with previous results using ether. We found that pentobarbitone required a much longer induction time than diethyl ether, which is suspected to be the cause of fluctuations in several haematological and blood chemical results. -
Enhanced Distillation • Use of Triangular Graphs
Lecture 15. Enhanced Distillation and Supercritical Extraction (1) [Ch. 11] • Enhanced Distillation • Use of Triangular Graphs - Zeotropic mixture -Mixture forming one minimum-boiling azeotrope - Mixture forming two minimum-boiling azeotropes • Residue-Curve Maps • Distillation-Curve Maps • Product-Composition Regions at Total Reflux Enhanced Distillation • Cases when ordinary distillation is not economical - Boiling point difference between components is less than 50℃ - Relative volatility is less than 1.10 - Mixture forms an azeotrope • Enhanced distillation - Extractive distillation : adding a large amount of solvent - Salt distillation : adding a soluble , ionic salt - Pressure-swing distillation : operating at two different pressures - Homogeneous azeotropic distillation : adding an entrainer - Heterogeneous azeotropic distillation : adding an entrainer - Reactive distillation : adding a separating agent to react selectively and reversibly with feed component(s) Zeotropic vs. Azeotropic Systems Binary zeotropic system Binary azeotropic system P = constant AtAzeotrope C T-y T-x Pure B xA, yA Pure A Use of Triangular Graphs • Triangular vapor-liquid diagram for ternary mixture - Too complex to understand • Plot with only equilibr ium liquid composition fofoatenayr a ternary mixture - Easy to understand -Convenient to use - Provide useful information in distillation of ternary components . Residue curve . Distill ati on curve Distillation Curves for Ternary Systems Each curve in each diagram is the locus of possible equilibrium liquid-phase -
Appendix D: Important Facts About Alcohol and Drugs
APPENDICES APPENDIX D. IMPORTANT FACTS ABOUT ALCOHOL AND DRUGS Appendix D outlines important facts about the following substances: $ Alcohol $ Cocaine $ GHB (gamma-hydroxybutyric acid) $ Heroin $ Inhalants $ Ketamine $ LSD (lysergic acid diethylamide) $ Marijuana (Cannabis) $ MDMA (Ecstasy) $ Mescaline (Peyote) $ Methamphetamine $ Over-the-counter Cough/Cold Medicines (Dextromethorphan or DXM) $ PCP (Phencyclidine) $ Prescription Opioids $ Prescription Sedatives (Tranquilizers, Depressants) $ Prescription Stimulants $ Psilocybin $ Rohypnol® (Flunitrazepam) $ Salvia $ Steroids (Anabolic) $ Synthetic Cannabinoids (“K2”/”Spice”) $ Synthetic Cathinones (“Bath Salts”) PAGE | 53 Sources cited in this Appendix are: $ Drug Enforcement Administration’s Drug Facts Sheets1 $ Inhalant Addiction Treatment’s Dangers of Mixing Inhalants with Alcohol and Other Drugs2 $ National Institute on Alcohol Abuse and Alcoholism’s (NIAAA’s) Alcohol’s Effects on the Body3 $ National Institute on Drug Abuse’s (NIDA’s) Commonly Abused Drugs4 $ NIDA’s Treatment for Alcohol Problems: Finding and Getting Help5 $ National Institutes of Health (NIH) National Library of Medicine’s Alcohol Withdrawal6 $ Rohypnol® Abuse Treatment FAQs7 $ Substance Abuse and Mental Health Services Administration’s (SAMHSA’s) Keeping Youth Drug Free8 $ SAMHSA’s Center for Behavioral Health Statistics and Quality’s (CBHSQ’s) Results from the 2015 National Survey on Drug Use and Health: Detailed Tables9 The substances that are considered controlled substances under the Controlled Substances Act (CSA) are divided into five schedules. An updated and complete list of the schedules is published annually in Title 21 Code of Federal Regulations (C.F.R.) §§ 1308.11 through 1308.15.10 Substances are placed in their respective schedules based on whether they have a currently accepted medical use in treatment in the United States, their relative abuse potential, and likelihood of causing dependence when abused.