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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. -
A Review of the Effect of Formic Acid and Its Salts on the Gastrointestinal
animals Review A Review of the Effect of Formic Acid and Its Salts on the Gastrointestinal Microbiota and Performance of Pigs Diana Luise * , Federico Correa , Paolo Bosi and Paolo Trevisi Department of Agricultural and Food Sciences (DISTAL), University of Bologna, 40127 Bologna, Italy; [email protected] (F.C.); [email protected] (P.B.); [email protected] (P.T.) * Correspondence: [email protected] Received: 20 April 2020; Accepted: 17 May 2020; Published: 19 May 2020 Simple Summary: Acidifiers, especially formic acid and its salts, have long been used for improving the gastrointestinal health and growth performance of pigs, especially piglets. Although, some biological mechanisms explaining their effects are already known, a lack of consensus is still reported on their effects on the gastrointestinal microbiome. The present review provides an overview and evaluation of the effects of formic acid and its salts on the gastrointestinal microbiota and on the growth performance of pigs. Abstract: Out of the alternatives to antibiotics and zinc oxide, organic acids, or simply acidifiers, play significant roles, especially in ensuring gut health and the growth performance of pigs. Regarding acidifiers, formic acid and its salts have shown very promising results in weaning, growing and finishing pigs. Although it is known that the main mechanisms by which acidifiers can improve livestock performance and health are related to the regulation of gastrointestinal pH, an improvement in intestinal digestibility and mineral utilization, and their antimicrobial properties against specific pathogens has been observed, while poor consensus remains in relation to the effect of acidifers on bacteria and the complex microbiome. -
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. -
Chemical Compatibility Storage Group
CHEMICAL SEGREGATION Chemicals are to be segregated into 11 different categories depending on the compatibility of that chemical with other chemicals The Storage Groups are as follows: Group A – Compatible Organic Acids Group B – Compatible Pyrophoric & Water Reactive Materials Group C – Compatible Inorganic Bases Group D – Compatible Organic Acids Group E – Compatible Oxidizers including Peroxides Group F– Compatible Inorganic Acids not including Oxidizers or Combustible Group G – Not Intrinsically Reactive or Flammable or Combustible Group J* – Poison Compressed Gases Group K* – Compatible Explosive or other highly Unstable Material Group L – Non-Reactive Flammable and Combustible, including solvents Group X* – Incompatible with ALL other storage groups The following is a list of chemicals and their compatibility storage codes. This is not a complete list of chemicals, but is provided to give examples of each storage group: Storage Group A 94‐75‐7 2,4‐D (2,4‐Dichlorophenoxyacetic acid) 94‐82‐6 2,4‐DB 609-99-4 3,5-Dinitrosalicylic acid 64‐19‐7 Acetic acid (Flammable liquid @ 102°F avoid alcohols, Amines, ox agents see SDS) 631-61-8 Acetic acid, Ammonium salt (Ammonium acetate) 108-24-7 Acetic anhydride (Flammable liquid @102°F avoid alcohols see SDS) 79‐10‐7 Acrylic acid Peroxide Former 65‐85‐0 Benzoic acid 98‐07‐7 Benzotrichloride 98‐88‐4 Benzoyl chloride 107-92-6 Butyric Acid 115‐28‐6 Chlorendic acid 79‐11‐8 Chloroacetic acid 627‐11‐2 Chloroethyl chloroformate 77‐92‐9 Citric acid 5949-29-1 Citric acid monohydrate 57-00-1 Creatine 20624-25-3 -
Thyl Triflates Using Aryl Formates As CO Surrogates
The Pd-Catalyzed Carbonylation Reaction of Naphthyl and Binaph- thyl Triflates Using Aryl Formates as CO Surrogates by Christina Grace Na A dissertation submitted in partial fulfillment of the requirements for the degree of Bachelor of Science (Honors Chemistry) in the University of Michigan 2015 Acknowledgements I want to start off by thanking my advisor Dr. Masato Koreeda, who has been an amazing mentor for me. My interest in chemistry, which was first fostered by Dr. John Montgomery in CHEM 210, was cemented after taking CHEM 215 taught by Dr. Koreeda. Dr. Koreeda has guided me with patience for close to three years now, and I can say confidently that I have been able to improve my techniques and critical thinking through my undergraduate research experience. Gratitude to my labmates, most notably Ryan Soheim and Caitlin Utt, for their company in the lab, and Emiko Nogami, a graduate student at Ochanomizu University, Tokyo, Japan, who was involved with the initial stage of the research on the carbonylation reaction as a visiting scholar during the month of August, 2014, in the laboratories of Professor Koreeda. In addition, I would like to thank all of my professors: Drs. Kathleen Nolta, Roseanne Sension, Zhan Chen, Kristina Hakansson, Brandon Ruotolo, Ted Goodson III, Raoul Kopelman, Bart Bartlett, Paul Zimmerman, Mark Banaszak Holl, Nathaniel Szymczak, John Wolfe, Corinna Schindler, and Pavel Nagorny, for their instruction and guidance. I’d like to extend a special thank you to Drs. Bart Bartlett and Brandon Ruotolo for their overall encouragement and for graciously writing my letters of recommendation despite their busy schedules. -
The Advances in Processes and Catalysts for the Production of Methyl Formate by Methanol Carbonylation – a Review
International Journal of Chemical & Petrochemical Technology (IJCPT) ISSN 2277-4807 Vol. 3, Issue 2, Jun 2013, 55-70 © TJPRC Pvt. Ltd. THE ADVANCES IN PROCESSES AND CATALYSTS FOR THE PRODUCTION OF METHYL FORMATE BY METHANOL CARBONYLATION – A REVIEW BIJAY N PATTANAIK R&D Centre, GNFC Ltd, Narmadanagar, Bharuch, Gujarat, India ABSTRACT Synthesis of methyl formate from six varieties of routes from different feed stocks is discussed. The commercial processes presently available for carbonylation of methanol to methyl formate using homogeneous catalyst (potassium methoxide /sodium methoxide) are summarized. This review also covers the advances in process technologies and research development to improve the efficiency of both homogeneous and heterogeneous catalysts for carbonylation of methanol to methyl formate. KEYWORDS: Methyl Formate, Methanol Carbonylation, Homogeneous Catalyst, Heterogeneous Catalyst, Anion Exchange Resins INTRODUCTION Methyl formate is one of the important chemical products of chemistry with varieties of applications. It is a versatile chemical precursor to a wide range of other chemicals such as formic acid, acetic acid, acetaldehyde, methyl acetate, ethylene glycol and formamide. The methyl formate is mainly used for production of formic acid by hydrolysis. The six routes for synthesis of methyl formate from different feed stocks are reported by Lee et.al[1].Presently industrial processes for production of methyl formate is dominated by methanol carbonylation using potassium methoxide /sodium methoxide catalyst[2]. Recent reported research studies to improve the current process technologies, alternative catalysts, both homogeneous and heterogeneous for carbonylation of methanol to methyl formate have been discussed. DIFFERENT ROUTES FOR METHYL FORMATE PRODUCTION Synthesis of methyl formate from six different routes is summarized in Figure 1.