Thyl Triflates Using Aryl Formates As CO Surrogates
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Trimethylacetic Formic Anhydride Precipitation from Ethanol and Diethyl Ether, M.P
PDF hosted at the Radboud Repository of the Radboud University Nijmegen The following full text is a publisher's version. For additional information about this publication click this link. http://hdl.handle.net/2066/16408 Please be advised that this information was generated on 2021-09-24 and may be subject to change. 460 Edward J. Vlietsira et al. / Trimethylacetic formic anhydride precipitation from ethanol and diethyl ether, m.p. 240°C (dec.); Acknowledgements [a]5 5 —140° (c 1.0, water). MS: M* 700. We thank Mr. P. Kranenburg for valuable technical as N-(6,14-endo-Etheno-7,8-dihydromorphine-7ai-carbonyl)-L- sistance and Messrs. J. A. de Groot, L. J. M. Helvensteijn -phenylalanyl-L-leucinol (14) and E. F. Lameijer for carrying out preliminary experi The hydrochloride of 12 (1.63 g, 2.4 mmol) was converted into the ments. We are grateful to the Management of Diosynth base and dissolved in 30 ml of anhydrous 2-propanol. To this B. V., Apeldoorn, The Netherlands, for gifts of chemicals. solution, 1.5 g (15 mmol) of anhydrous calcium chloride and We thank the U.S.A. Committee on Problems of Drug 1.14 g (30 mmol) of sodium tetrahydroborate were added. The Dependence and Dr. A. E. Jacobson, Biological Coordi conversion was complete (TLC) after 6 days at 35°C. Water nator, for the results of the pharmacological studies. We (50 ml) was then added and the mixture acidified with 2 N hydro gen chloride to pH 2-3. Extraction with a mixture of chloroform are indebted to Dr. -
Methyl Formate
SIGMA-ALDRICH sigma-aldrich.com Material Safety Data Sheet Version 5.0 Revision Date 09/17/2012 Print Date 03/13/2014 1. PRODUCT AND COMPANY IDENTIFICATION Product name : Methyl formate Product Number : 291056 Brand : Sigma-Aldrich Supplier : Sigma-Aldrich 3050 Spruce Street SAINT LOUIS MO 63103 USA Telephone : +1 800-325-5832 Fax : +1 800-325-5052 Emergency Phone # (For : (314) 776-6555 both supplier and manufacturer) Preparation Information : Sigma-Aldrich Corporation Product Safety - Americas Region 1-800-521-8956 2. HAZARDS IDENTIFICATION Emergency Overview OSHA Hazards Flammable liquid, Target Organ Effect, Harmful by ingestion., Irritant Target Organs Eyes, Kidney GHS Classification Flammable liquids (Category 1) Acute toxicity, Oral (Category 4) Acute toxicity, Inhalation (Category 4) Eye irritation (Category 2A) Specific target organ toxicity - single exposure (Category 3) GHS Label elements, including precautionary statements Pictogram Signal word Danger Hazard statement(s) H224 Extremely flammable liquid and vapour. H302 + H332 Harmful if swallowed or if inhaled H319 Causes serious eye irritation. H335 May cause respiratory irritation. Precautionary statement(s) P210 Keep away from heat/sparks/open flames/hot surfaces. - No smoking. P261 Avoid breathing dust/ fume/ gas/ mist/ vapours/ spray. P305 + P351 + P338 IF IN EYES: Rinse cautiously with water for several minutes. Remove contact lenses, if present and easy to do. Continue rinsing. HMIS Classification Health hazard: 2 Sigma-Aldrich - 291056 Page 1 of 7 Chronic Health Hazard: * Flammability: 4 Physical hazards: 0 NFPA Rating Health hazard: 2 Fire: 4 Reactivity Hazard: 0 Potential Health Effects Inhalation May be harmful if inhaled. Causes respiratory tract irritation. Skin Harmful if absorbed through skin. -
UC Irvine UC Irvine Electronic Theses and Dissertations
UC Irvine UC Irvine Electronic Theses and Dissertations Title Steps Toward CO2 Reduction to Methanol via Electrochemical Cascade Catalysis Permalink https://escholarship.org/uc/item/4wx6g1vm Author Mercer, Ian Patrick Publication Date 2020 License https://creativecommons.org/licenses/by/4.0/ 4.0 Peer reviewed|Thesis/dissertation eScholarship.org Powered by the California Digital Library University of California UNIVERSITY OF CALIFORNIA, IRVINE Steps Toward CO2 Reduction to Methanol via Electrochemical Cascade Catalysis THESIS submitted in partial satisfaction of the requirements for the degree of MASTER OF SCIENCE in Chemistry by Ian Patrick Mercer Dissertation Committee: Professor Jenny Y. Yang, Chair Professor William J. Evans Professor Andy S. Borovik 2020 © 2020 Ian Patrick Mercer ii Table of Contents Acknowledgements iv Abstract v Chapter 1: Methyl Formate and Formaldehyde Reduction by Metal Hydrides 1 Chapter 2: Synthesis of Group 8 Metal Complexes of LDMA for the Study of Outer Sphere Interactions 25 Conclusion 33 Experimental 34 References 37 iii Acknowledgements I would like to express my sincere appreciation to my committee, especially my chair, Professor Jenny Y. Yang. Her commitment to science, mentoring, and ‘doing the right thing’ will forever inspire me. Financial support was provided by the University of California, Irvine and US Department of Energy, Office of Science, Office of Basic Energy Sciences Awards DE-SC0012150 and DE- 0000243266. iv Abstract of the Thesis Steps Toward CO2 Reduction to Methanol via Electrochemical Cascade Catalysis by Ian Patrick Mercer Master of Science in Chemistry University of California, Irvine, 2020 Professor Jenny Y. Yang, Chair Research on two independent projects is presented: (1) Homogeneous cascade catalysis has been used for the hydrogenation of CO2 to methanol as it allows for rational tuning of catalyst reactivity and lower reaction temperatures compared to heterogeneous catalysis. -
Process for Producing Methyl Methacrylate Verfahren Zur Herstellung Von Methylmethacrylat Procede Pour La Fabrication De Methacrylate De Methyle
~™ II 1 1 III II II 1 1 II II I Ml II I II I II (19) J European Patent Office Office europeen des brevets (11) EP 0 406 676 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publicationation and mention (51 ) |nt. CI.6: C07C 69/54, C07C 67/20 of the grant of the patent: 27.03.1996 Bulletin 1996/13 (21) Application number: 90112194.7 (22) Date of filing: 27.06.1990 (54) Process for producing methyl methacrylate Verfahren zur Herstellung von Methylmethacrylat Procede pour la fabrication de methacrylate de methyle (84) Designated Contracting States: • Ebata, Shuji, DE ES FR GB IT NL C/o Mitsubishi Gas Chem. Com. Tayuhama, Niigata-shi, Niigata-ken (JP) (30) Priority: 04.07.1989 JP 171190/89 (74) Representative: Turk, Gille, Hrabal, Leifert (43) Date of publication of application: Brucknerstrasse 20 09.01.1991 Bulletin 1991/02 D-40593 Dusseldorf (DE) (73) Proprietor: MITSUBISHI GAS CHEMICAL (56) References cited: COMPANY, INC. DE-A- 3 436 608 Chiyoda-ku, Tokyo (JP) • PATENT ABSTRACTS OF JAPAN vol. 14, no. 68 (72) Inventors: (C- 686)(401 1 ), 8 February 1 990; & JP-A-1 290653 • Higuchi, Hirofumi, (MITSUBISHI GAS CHEM) 22.11. 1989 C/o Mitsubishi Gas Chem. Com. Tayuhama, Niigata-shi, Niigata-ken (JP) Remarks: • Kida, Koichi, The file contains technical information submitted C/o Mitsubishi Gas Chem. Com. after the application was filed and not included in this Tayuhama, Niigata-shi, Niigata-ken (JP) specification CO CO CO o Note: Within nine months from the publication of the mention of the grant of the European patent, any person may give notice to the European Patent Office of opposition to the European patent granted. -
Process of Formic Acid Production by Hydrolysis
(19) TZZ ¥_T (11) EP 2 747 883 B1 (12) EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) Int Cl.: of the grant of the patent: B01J 14/00 (2006.01) C07C 51/09 (2006.01) 15.02.2017 Bulletin 2017/07 C07C 53/02 (2006.01) B01J 10/00 (2006.01) B01D 3/10 (2006.01) C07C 51/44 (2006.01) (21) Application number: 12751504.7 (86) International application number: (22) Date of filing: 27.08.2012 PCT/EP2012/066622 (87) International publication number: WO 2013/030162 (07.03.2013 Gazette 2013/10) (54) PROCESS OF FORMIC ACID PRODUCTION BY HYDROLYSIS OF METHYL FORMATE VERFAHREN ZUR HERSTELLUNG VON AMEISENSÄURE DURCH HYDROLYSE VON METHYLFORMIAT PROCÉDÉ DE PRODUCTION D’ACIDE FORMIQUE PAR HYDROLYSE DE FORMIATE DE MÉTHYLE (84) Designated Contracting States: • TREJBAL, Jiri AL AT BE BG CH CY CZ DE DK EE ES FI FR GB 278 01 Kralupy nad Vltavou (CZ) GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO • ROOSE, Peter PL PT RO RS SE SI SK SM TR 9831 Sint-Martens-Latem (BE) (30) Priority: 27.08.2011 US 201161528204 P (74) Representative: Gevers Patents Intellectual Property House (43) Date of publication of application: Holidaystraat 5 02.07.2014 Bulletin 2014/27 1831 Diegem (BE) (73) Proprietor: Taminco (56) References cited: 9000 Gent (BE) WO-A1-00/39067 US-A- 4 262 140 US-B1- 6 713 649 US-B2- 6 696 603 (72) Inventors: • PASEK, Josef 160 00 Praha 6 (CZ) Note: Within nine months of the publication of the mention of the grant of the European patent in the European Patent Bulletin, any person may give notice to the European Patent Office of opposition to that patent, in accordance with the Implementing Regulations. -
Methyl Formate Mfm
METHYL FORMATE MFM CAUTIONARY RESPONSE INFORMATION 4. FIRE HAZARDS 7. SHIPPING INFORMATION 4.1 Flash Point: -26°F C.C. 7.1 Grades of Purity: Technical, practical, and Common Synonyms Liquid Colorless Pleasant odor 4.2 Flammable Limits in Air: 5%-22.7% spectro grades: all 97.5+% Formic acid, methyl ester 4.3 Fire Extinguishing Agents: Dry 7.2 Storage Temperature: <85°F Mixes with water. Flammable, irritating vapor is produced. Boiling point chemical, alcohol foam, carbon dioxide 7.3 Inert Atmosphere: No requirement is 88°F. 4.4 Fire Extinguishing Agents Not to Be 7.4 Venting: Pressure-vacuum Used: Water may be ineffective. 7.5 IMO Pollution Category: D Evacuate. 4.5 Special Hazards of Combustion Keep people away. Products: Not pertinent 7.6 Ship Type: 2 Shut off ignition sources. Call fire department. 4.6 Behavior in Fire: Vapor is heavier than 7.7 Barge Hull Type: Currently not available Notify local health and pollution control agencies. air and may travel considerable distance to a source of ignition and flash back. FLAMMABLE. 8. HAZARD CLASSIFICATIONS Fire 4.7 Auto Ignition Temperature: 853°F Containers may explode in fire. 8.1 49 CFR Category: Flammable liquid Flashback along vapor trail may occur. 4.8 Electrical Hazards: Currently not 8.2 49 CFR Class: 3 Vapor may explode if ignited in an enclosed area. available Extinguish with dry chemicals, alcohol foam, or carbon dioxide. 4.9 Burning Rate: 2.5 mm/min. 8.3 49 CFR Package Group: I Water may be ineffective on fire. 4.10 Adiabatic Flame Temperature: Currently 8.4 Marine Pollutant: No Cool exposed containers with water. -
Working Fluid Selection for Space-Based Two-Phase Heat Transport Systems
NBSIR 88-3812 Working Fluid Selection for Space-Based Two-Phase Heat Transport Systems Mark O. McLinden U.S. DEPARTMENT OF COMMERCE National Bureau of Standards Gaithersburg, MD 20899 May 1988 Issued August 1988 75 Years Stimulating America's Progress 1913-1988 Prepared for: National Aeronautics and Space Administration Goddard Space Flight Center NBSIR 88-3812 WORKING FLUID SELECTION FOR SPACE-BASED TWO-PHASE HEAT TRANSPORT SYSTEMS Mark O. McLinden U.S. DEPARTMENT OF COMMERCE National Bureau of Standards Gaithersburg, MD 20899 May 1988 Issued August 1988 Prepared for: National Aeronautics and Space Administration Goddard Space Flight Center U.S. DEPARTMENT OF COMMERCE, C. William Verity, Secretary NATIONAL BUREAU OF STANDARDS, Ernest Ambler, Director , ABSTRACT The working fluid for externally-mounted, space-based two-phase heat transport systems is considered. A sequence of screening criteria involving freezing and critical point temperatures and latent heat of vaporization and vapor density are applied to a data base of 860 fluids. The thermal performance of the 52 fluids which pass this preliminary screening are then ranked according to their impact on the weight of a reference system. Upon considering other non-thermal criteria ( f lagimability toxicity and chemical stability) a final set of 10 preferred fluids is obtained. The effects of variations in system parameters is investigated for these 10 fluids by means of a factorial design. i * . I . INTRODUCTION In order to remove the heat generated by electronics and other payloads on spacecraft some type of heat transport system is required. The heat generating equipment is typically attached to a 'cold plate'. -
VAPOR-LIQUID EQUILIBRIUM DATA COLLECTION Chemistry Data Series
J. Gmehling U. Onken VAPOR-LIQUID EQUILIBRIUM DATA COLLECTION Esters Supplement 2 Chemistry Data Series Vol. I, Part 5b Published by DECHEMA Gesellschaft fur Chemische Technik und Biotechnologie e. V. Executive Editor: Gerhard Kreysa Bibliographic information published by Die Deutsche Bibliothek Die Deutsche Bibliothek lists this publication in the Deutsche Nationalbibliographie; de tailed bibliographic data is available on the Internet at http://dnb.ddb.de ISBN: 3-89746-041-6 © DECH EMA Gesellschaft fOr Chemische Te chnik und Biotechnologie e. V. Postfach 15 01 04, D-60061 Frankfurt am Main, Germany, 2002 Dieses Werk ist urheberrechtlich geschutzt. Alle Rechte, auch die der Obersetzung, des Nachdrucks und der Vervielfi:Htigung des Buches oder Teilen daraus sind vorbehalten. Kein Teil des Werkes darf ohne schriftliche Genehmigung der DECHEMA in irgendeiner Form (Fotokopie, Mikrofilm oder einem anderen Verfahren), auch nicht fOr Zwecke der Un terrichtsgestaltung, reproduziert oder unter Verwendung elektronischer Systeme verarbei tet, vervielfaltigt oder verbreitet werden. Die Herausgeber Obernehmen fOr die Richtigkeit und Vollstandigkeit der publizierten Daten keinerlei Gewahrleistung. This work is subject to copyright. All rights are reserved, whether the whole or part of the material is concerned, including those of translation, reprinting, reproduction by photo copying machine or similar means. No partof this work may be reproduced, processed or distributed in any form, not even for teaching purposes - by photocopying, microfilm or other processes, or implemented in electronic information storage and retrieval systems - without the written permission of the publishers. The publishers accept no liability for the accuracy and completeness of the published data. This volume of the Chemistry Data Series was printed using acid-free paper. -
Oxygenated Fuel from Bio-Oil Via Methylation of Acids and Phenolics
Oxygenated Fuel from Bio-oil via Methylation of Acids and Phenolics Suh-Jane Lee, Evgueni Polikarpov, Huamin Wang and Karl Albrecht Chemical and Biological Process Development Group Pacific Northwest National Laboratory 902 Battelle Blvd., Richland, WA 99352, USA 1 Background The Co-Optimization of Fuels and Engines (Co-Optima) project is a collaborative project between national labs, universities and industry to develop new fuels and engine architectures in tandem to maximize performance and carbon efficiency with low GHGs emission. Objectives for Future Fuels: 1. Reduce petroleum consumption 2. Improve fuel economy 3. Decrease pollutants and GHG emission 4. Accelerate the speed of advanced biofuel deployment 2 Future Fuels-Oxygenated Fuel 1. Advantages a. No need for addition of hydrogen to remove oxygen during upgrading process b. Atom efficiency without loss of oxygen c. Enhance Octane Number 2. Market interests: “Industry is experiencing an Octane lovefest; Petroleum marketers have talked about higher octane demand for future fuels.” -Ron Lamberty in the April, 2016 issue of EPM 3. Aryl ethers are particularly effective anti-knock additives for gasolines. Dolhyj et al. USA Patent 4,412,847, 1983“ Motor Fuel Additive” Compound RON MON AKI (R+M)/2 n-Octane -20 n-Heptane 0 0 0 n-hexane 25 26.0 26 n-pentane 62 61.9 62 ethanol 107 n-butanol 92 71 83 Methyl acetate >120 Anisole 103 Methyl acetate as a component octane commercial gasoline by Amirkhanow K. Sh. and Kislitsyn, A. A. Oil and Gas Business, 2014, 1, 178-192 3 Esters and Aryl Ethers from Bio-oil? 1. -
1,3-Butadiene: Human Health Aspects
This report contains the collective views of an international group of experts and does not necessarily represent the decisions or the stated policy of the United Nations Environment Programme, the International Labour Organization, or the World Health Organization. Concise International Chemical Assessment Document 30 1,3-BUTADIENE: HUMAN HEALTH ASPECTS Please note that the layout and pagination of this pdf file are not identical to those of the printed CICAD First draft prepared by K. Hughes, M.E. Meek, M. Walker, and R. Beauchamp, Health Canada, Ottawa, Canada Published under the joint sponsorship of the United Nations Environment Programme, the International Labour Organization, and the World Health Organization, and produced within the framework of the Inter-Organization Programme for the Sound Management of Chemicals. World Health Organization Geneva, 2001 The International Programme on Chemical Safety (IPCS), established in 1980, is a joint venture of the United Nations Environment Programme (UNEP), the International Labour Organization (ILO), and the World Health Organization (WHO). The overall objectives of the IPCS are to establish the scientific basis for assessment of the risk to human health and the environment from exposure to chemicals, through international peer review processes, as a prerequisite for the promotion of chemical safety, and to provide technical assistance in strengthening national capacities for the sound management of chemicals. The Inter-Organization Programme for the Sound Management of Chemicals (IOMC) was established in 1995 by UNEP, ILO, the Food and Agriculture Organization of the United Nations, WHO, the United Nations Industrial Development Organization, the United Nations Institute for Training and Research, and the Organisation for Economic Co-operation and Development (Participating Organizations), following recommendations made by the 1992 UN Conference on Environment and Development to strengthen cooperation and increase coordination in the field of chemical safety. -
WO 2013/057196 Al 25 April 2013 (25.04.2013) P O P C T
(12) INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property Organization International Bureau (10) International Publication Number (43) International Publication Date WO 2013/057196 Al 25 April 2013 (25.04.2013) P O P C T (51) International Patent Classification: (81) Designated States (unless otherwise indicated, for every C07D 501/36 (2006.01) A61P 31/04 (2006.01) kind of national protection available): AE, AG, AL, AM, A61K 31/546 (2006.01) AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DK, DM, (21) Number: International Application DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, PCT/EP2012/070664 HN, HR, HU, ID, IL, IN, IS, JP, KE, KG, KM, KN, KP, (22) International Filing Date: KR, KZ, LA, LC, LK, LR, LS, LT, LU, LY, MA, MD, 18 October 2012 (18.10.2012) ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, NI, NO, NZ, OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, (25) Filing Language: English RW, SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, TH, TJ, (26) Publication Language: English TM, TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW. (30) Priority Data: 11185954.2 20 October 201 1 (20. 10.201 1) EP (84) Designated States (unless otherwise indicated, for every kind of regional protection available): ARIPO (BW, GH, (71) Applicant: DSM SINOCHEM PHARMACEUTICALS GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, SZ, TZ, NETHERLANDS B.V. -
Ethyl Formate Fumigation an Overview Update
11th International Working Conference on Stored Product Protection Ethyl formate fumigation an overview update Ryan, R.F*#1, De Lima, C.P.F.2 1VAPORFAZE, PO Box 4, Sans Souci NSW 2219, Australia 2Consultant Research Entomologist, Perth WA, Australia *Corresponding author, Email: [email protected] #Presenting author, Email: [email protected] DOI: 10.14455/DOA.res.2014.161 Abstract The historical fumigant ethyl formate [EF] is proving to be a methyl bromide alternative. EF effectiveness against dried fruit insects was published in 1925. Non-flammable mixture of EF (14.4 vol% EF) with carbon dioxide [CO2] was reported by Jones (1933). On-site mixing of EF liquid into a stream of CO2 in export grain structures was trialed by Allen and Desmarchelier (2000). In addition to eliminating the flammability hazard, CO2 has a synergistic effect with an optimal range of 5-20%. Ryan and Bishop (2002) developed a commercial mixture of EF dissolved in liquid CO2which was compressed to 40 bar pressure in an industrial gas cylinder. EF is a highly flammable volatile liquid (b.pt.=54°C) which requires vaporization to minimize adsorption and achieve uniform distribution throughout the fumigation space. Pre- or post (on- site) EF/CO2 mixture is converted to a gaseous mixture using a proprietary high pressure vaporiser. The EF/CO2 gaseous mixture is accurately dispensed into the fumigation chambers by weighing. However, because the application rate of the EF/CO2 mixture is between 75 and 420 g/m3 fumigations need to be done in adequately tested gas-tight structures (De Lima et al., 1994) while vacuum chambers are generally satisfactory.