PATENT OFFICE 2,101,820 PROCESS for the PREPARATION of POLYMERIZABLE UNSATURATED COM POUNDS John C

Total Page:16

File Type:pdf, Size:1020Kb

PATENT OFFICE 2,101,820 PROCESS for the PREPARATION of POLYMERIZABLE UNSATURATED COM POUNDS John C Patented Dec. 7, 1937 2,101,820 UNITED STATES PATENT OFFICE 2,101,820 PROCESS FOR THE PREPARATION OF POLYMERIZABLE UNSATURATED COM POUNDS John C. Woodhouse, Wilmington, Del, assignor to E. I. du Pont de Nemours & Company, Will mington, Del, a corporation of Delaware No Drawing. Application December 5, 1933, Serial No. 701,053 10 Claims. (Cl. 260-106) This invention relates to a process for the prep included under the term aryl include benzyl, aration of unsaturated polymerizable organic naphthyl, and analogous aryl compounds. It will compounds and more particularly to the prepara be appreciated by those skilled in this art that tion of Such compounds from Saturated organic altho the Substitutions in the X and Y positions 5 compounds containing an isopropyl radical at Will alter the reaction rates and in many in 5 tached to a carbonyl group which likewise carries stances the by-products resulting from the de a hydrogen, hydroxy, aryl, or aralkyl group. hydrogenation, these substitutions are to be given An object of the present invention is to provide but secondary consideration for, generally speak an improved process for the preparation of poly ing, if the compound to be dehydrogenated has the O merizable unsaturated aliphatic and/or aromatic basic formula 10 organic compounds. Another object of the in vention is to provide an improved process for the chi-qi- - O preparation of esters of the unsaturated mono it may be dehydrogenated to an unsaturated poly carboxylic aliphatic organic acids. Another ob merizable compound. ject of the invention is to provide an improved The compounds containing an isobutyryl group, 15 process for the preparation of methacrylic acid. such, for example, as isobutyric acid, isobutyralde A further object of the invention is to provide a hyde, or an alkyl ester of isobutyric acid, such, process for the preparation of polymerizable esters for example, as methyl isobutyrate, ethyl iso of the unsaturated monocarboxylic aliphatic Or butyrate and the higher esters thereof, are par ganic acids from aliphatic or aromatic organic ticularly well suited for dehydrogenation in ac 20 compounds containing an isopropyl radical at cord with my process in which corresponding tached to a carbonyl group which likewise carries unsaturated polymerizable compounds are ob a hydrogen, a hydroxy, an alkyl, or an aryl group. tained; that is from isobutyryl aldehyde there is A further object of the invention is to provide obtained an alpha methylacrolein which may be a process for the preparation of the methyl ester directly polymerized or which may be oxidized 25 of methacrylic acid including the steps of catalyti and then esterified to the polymerizable meth cally dehydrogenating a compound containing an acrylate; from isobutyric acid, methacrylic acid iscbutyryl group and Subsequently converting the which may be esterified to the ester; and in some thus obtained oxygenated compound to an alkyl instances from the alkyl esters of isobutyric acid ester of methacrylic acid. Other objects and ad the corresponding alkyl methacrylates are ob 30 Vantages Will hereinafter appear. tained directly. I usually prefer to convert the Waluable polymerizable unsaturated compounds unsaturated compounds, if in the form of an are produced by dehydrogenation in accord with aldehyde or acid, to the ester prior to polymer my invention and Substantially as indicated by ization. M the equation: Polymerization may be effected by any of the 35 customary processes such, for example, as by heating, submitting the unsaturated compound X Y X Y to ultraViolet light, etc. Heat and/or light treat in which X may be an alkyl or aryl group and ment may be augmented by the addition of per 4) Y may be hydrogen, or a hydroxyl, alkoxy, aryl, oxides, if desired. 40 alkyl, or aralkyl group. Thus by substituting an The dehydrogenation of the above compounds I alkyl group Such as methyl, ethyl, propyl or a prefer, generally, to effect in the vapor phase. higher group for X and hydrogen for Y - iso Isobutyraldehyde, for example, is vaporized and butyryl aldehyde, 2-methyl butyryl, aldehyde, passed at a temperature within the range of and analogous aldehydes are indicated; these 200-500 C., over a suitable dehydrogenation 45 - compounds being dehydrogenated to alpha catalyst. The dehydrogenation may be conducted methyl acrolein, alpha-ethyl acrolein, respective also under elevated pressures, although usually ly, etc.; by the substitution of a hydroxyl group I prefer to carry out the reaction under atmos in lieu of hydrogen there would result 2-methyl pheric pressure. A number of dehydrogenation propionic acid, 2-ethyl propionic acid, etc., which catalysts may be employed for the treatment of upon dehydrogenation would be converted re isobutyryl containing compounds and the other spectively to methacrylic and ethylacrylic acids. compounds indicated above including, for ex The specific groups included under alkoxy cover, ample, nickel, copper, platinum, etc., the com for example, methoxy, ethoxy, propoxy and the pound catalysts such as copper-zinc-cadmium, 5 5 higher alkyloxy compounds, while the compounds copper chromite, and like well known catalysts. 2 2,101,820 I shall now describe several examples illus hyde by passing it in the vapor phase over a trating my invention which, however, will be un copper-chromium-zinc-cadmium catalyst at a derstood to limit in no way the Operating cond temperature of approximately 400° C. tions, equivalents, or Scope thereof. 4. A process of preparing an alkyl ester of Eacample 1.-Substantially anhydrous isobutyr methacrylic acid which conprises dehydrogenat aldehyde was passed at atmospheric pressure and ing isobutyraldehyde by passing it in the vapor at a temperature of approximately 400° C. Over phase Over a dehydrogenation catalyst at a tem 100 cc. charge of 8-14 mesh copper-chromium perature between 200 and 500 C., and subse zinc-cadmium catalyst at a space velocity of ap quently Oxidizing and esterifying the alpha 0. proximately 145. The catalyst may be prepared methyl acrolein to an ester of methacrylic acid. 10 in accord with the patented process of Lazier, 5. In a process for the preparation of poly described in U. S. Patent No. 1,964,001. The exit merizable esters of methacrylic acid the step gas issuing from the catalytic reaction was led which comprises dehydrogenating isobutyralde thru a water condenser, and a cold trap cooled hyde at a temperature of between 200 and 500 5 in a solid carbon dioxide-methanol bath. The C. in the presence of a dehydrogenation catalyst. 5 exit gas was collected by displacement of water. 6. A process of preparing a methyl ester of A total condensate of 116 cc, was collected from methacrylic acid which comprises dehydro the dehydrogenation of a 1.31 mols of isobutyr genating isobutyraldehyde by passing it in the aldehyde which contained an appreciable quan vapor phase over a dehydrogenation catalyst at tity of alpha-methyl acrolein, which is readily a temperature between 200 and 500° C., and sub 20 converted to the methyl ester of methacrylic acid Sequently oxidizing the product and esterifying by oxidation followed by esterification-well the Oxidation product with methanol. known oxidation and esterification processes may 7. In a process for the preparation of poly be used. merizable unsaturated organic compounds select 25 Eacample 2.-After drying isobutyraldehyde ed from the group consisting of alpha-aryl and 25 over anhydrous calcium chloride and distilling, alpha-alkyl Substituted acrylic acid compounds the thus dehydrated isobutyraldehyde, boiling be the step which comprises dehydrogenating, in the tween 63-64 C., was passed over a catalyst simi presence of a dehydrogenation catalyst, a com lar to that disclosed in Example 1 at a tempera pound in accord with the following equation: 30 ture of approximately 464 C., a space velocity of 30 approximately 118, and at atmospheric pressure. 2CH-H--0-2CH---0+H, 36 cc, of condensate was collected from the pas k H. kh sage of .526 gram mol. Of the oldehyde in a man in which X is a radical selected from the group ner similar to that disclosed in Example i. The consisting of alkyl and aryl radicals. 35 condensate contained alpha-methyl acrolein, 8. In a process for the preparation of poly 35 which on treatment in the liquid phase With nerizable unsaturated organic compounds select potassium dichromate and dilute sulfuric acid ed from the group consisting of alpha-aryl and may be converted to methyl acrylic acid, which alpha-alkyl substituted acrylic acid compounds, in turn is esterified in the usual manner with an the step which comprises reacting a compound aliphatic alcohol to obtain an alkyl ester of having the basic formula: methacrylic acid. From a consideration of the above Specifica chi-gh- O tion, it will be realized that any modification or k h improvement of the process herein described will in which X is a radical selected from the group come within the scope of my invention without consisting of alkyl radicals and aryl radicals, in sacrificing any of the advantages that may be the presence of a dehydrogenating catalyst. 45 derived therefron. 9. In a process for the preparation of an alkyl I claim: ester of methacrylic acid, the steps which com 1. In a process for the preparation of poly prise dehydrogenating a compound selected from merizable esters of methacrylic acid, the step the group consisting of isobutyraldehyde, iso which comprises dehydrogenating 'at reaction butyric acid, and its esters by passing the com 50 temperature isobutyraldehyde to alpha methyl pound in the vapor phase over a dehydrogenation acrolein in the presence of a dehydrogenating catalyst at a temperature between 200 and 500° catalyst. C. 2. In a process for the preparation of poly 10. In a process for the preparation of poly merizable esters of methacrylic acid, the steps merizable esters of methacrylic acid, the steps which comprise dehydrogenating isobutyralde which comprise dehydrogenating a compound hyde to alpha-methyl acrolein at a temperature selected from the group consisting of isobutyral of 200-500° C., and in the presence of a dehydro dehyde, isobutyric acid and its esters by passing genation catalyst adapted to the reaction.
Recommended publications
  • Acid-Base Properties, Deactivation, and in Situ Regeneration of Condensation Catalysts for Synthesis of Methyl Methacrylate
    ACID-BASE PROPERTIES, DEACTIVATION, AND IN SITU REGENERATION OF CONDENSATION CATALYSTS FOR SYNTHESIS OF METHYL METHACRYLATE MAKARAND R. GOGATE', JAMES J. SPIVEY', AND JOSEPH R. ZOELLER2 'Research Triangle Institute, 3040 Cornwallis Road, RTP, NC 27709-2 194 2Eastman Chemical Company, Kingsport, TN, 37662-5 150 ABSTRACT Condensation reaction of a propionate with formaldehyde is a novel route for synthesis of methyl methacrylate (MMA). The reaction mechanism involves a proton abstraction from the propionate on the basic sites and activation of the aliphatic aldehyde on the acidic sites of the catalyst. The acid-base properties of ternary V-Si-P oxide catalysts and their relation to the MMA yield in the vapor phase condensation of formaldehyde with propionic anhydride has been studied for the first time. Five different V-Si-P catalysts with different atomic ratios of vanadium, silicon, and phosphorous were synthesized, characterized, and tested in a fixed-bed microreactor system. A V-Si-P 1:10:2.8 catalyst gave the maximum condensation yield of 56% based on HCHO fed at 300 "C and 2 atm and at a space velocity of 290 cc/g cateh. A parameter called the "q-ratio" has been defined to correlate the condensation yields to the acid-base properties. The correlation of q-ratio with the condensation yield shows that higher q-ratios are more desirable. The long-term deactivation studies on the V-Si-P 1: 10:2.8 catalyst at 300 "C and 2 atm and at a space velocity of 290 cc/g cat-h show that the catalyst activity drops by a factor of nearly 20 over a 180 h period.
    [Show full text]
  • Submitted To
    I 1 RTI PROJECT NO. 9611-6048 DOE Contract No. DE-AC22-94PC94065 January 1,1995 through March 31,1995 SYNTHESIS OF ACRYLATES AND METHACRLYATES FROM COAL-DERIVED SYNGAS Quarterly Technical Progress Report Submitted to US. Department of Energy Pittsburgh Energy Technology Center P. 0. Box 10940 Pittsburgh, Pennsylvania 15236-0940 Submitted by Research Triangle Institute P. 0. Box 12194 Research Triangle Park, NC 27709 DOE COR: Richard E. Tischer RTI Project Manager: James J. Spivey DISCLAIMER This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsi- bility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Refer- ence herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recom- mendation, or favoring by the United States Government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the DiCJTRlBfllQN THIS DOWMENT mm United States Government or any agency thereof. OF %”/ - DISCLAIMER Portions of this document may be illegible in electronic image products. Images are produced from the best available original document. Executive Summary Task 1-Synthesis of Propionates The objective of this Task is to develop the technology for the synthesis of low-cost propionates.
    [Show full text]
  • The Effect of Cation Type and H+ on the Catalytic Activity of the Keggin Anion [Pmo12o40]3- in the Oxidative Dehydrogenation Of
    Journal of Catalysis 195, 360–375 (2000) doi:10.1006/jcat.2000.2987, available online at http://www.idealibrary.com on The Effect of Cation Type and H+ on the Catalytic Activity 3 of the Keggin Anion [PMo12O40] in the Oxidative Dehydrogenation of Isobutyraldehyde Ji Hu and Robert C. Burns1 School of Biological and Chemical Sciences, The University of Newcastle, Callaghan 2308, Australia Received March 23, 2000; revised July 4, 2000; accepted July 5, 2000 such as the oxidative dehydrogenation of isobutyric acid The oxidative dehydrogenation of isobutyraldehyde to metha- and the oxidation of methacrolein, both of which yield 3 crolein over [PMo12O40] -containing catalysts has been shown to methacrylic acid (1–5). Methacrylic acid is, in turn, reacted proceed through bulk catalysis-type II, which depends on the rates with methanol to yield methyl methacrylate, an extremely + of diffusion of the redox carriers (H and e ) into the catalyst bulk. important acrylic monomer, which is then polymerized to Variations in catalyst behaviour have been shown to change with give poly(methyl methacrylate). Heteropolyoxometalates the countercation and appear to be related to the polarizing abil- are also active acid catalysts, and processes based both on ity of the cation, which can be represented by the ionic potential their redox and acid–base properties have found commer- (charge/ionic radius). This, in turn, may indicate that the active 3 cial applications (3–5). site at the [PMo12O40] ion is close to an attendant countercation. For the alkali metal ions Li+,Na+,K+,Rb+, and Cs+ as well as the The study of heteropolyoxometalates as oxidation– (isoelectronic) ions of the series Cs+,Ba2+,La3+, and Ce4+, the stud- reduction catalysts has involved primarily Keggin-based 3 ies have shown that conversion generally decreases with increasing structures, principally [PMo12O40] , as well as substi- ionic potential, while selectivity to methacrolein is less affected by tuted species involving replacement of one or more changes in this property.
    [Show full text]
  • Design and Optimization of a Process for the Production of Methyl Methacrylate Via Direct Methylation
    processes Article Design and Optimization of a Process for the Production of Methyl Methacrylate via Direct Methylation Taotao Liang 1,2, Xiaogang Guo 2,3,*, Abdulmoseen Segun Giwa 1,4, Jianwei Shi 3, Yujin Li 3, Yan Wei 3, Xiaojuan Wang 5, Xuansong Cao 3, Xiaofeng Tang 3 and Jialun Du 3 1 Green Intelligence Environmental School, Yangtze Normal University, Chongqing 408003, China; [email protected] (T.L.); [email protected] (A.S.G.) 2 Faculty of Materials and Energy, Southwest University, Chongqing 400715, China 3 College of Chemistry and Chemical Engineering, Yangtze Normal University, Chongqing 408003, China; [email protected] (J.S.); [email protected] (Y.L.); [email protected] (Y.W.); [email protected] (X.C.); [email protected] (X.T.); [email protected] (J.D.) 4 State Key Joint Laboratory of Environment Simulation and Pollution Control, School of Environment, Tsinghua University, Beijing 100084, China 5 College of chemistry and bioengineering, Guilin University of Technology, Guilin 541004, China; [email protected] * Correspondence: [email protected]; Tel.: +86-023-72782170 Received: 25 April 2019; Accepted: 6 June 2019; Published: 18 June 2019 Abstract: Methyl methacrylate (MMA) plays a vital role in national productions with broad application. Herein, the production of MMA is realized by the improved eco-friendly direct methylation method using Aspen Plus software. Three novel kinds of energy-saving measures were proposed in this study, including the recycle streams of an aqueous solution, methacrolein (MAL), and methanol, the deployment of double-effect distillation instead of a normal one, and the design of a promising heat-exchange network.
    [Show full text]
  • Methacrylic Acid, CAS No. 79-41-4; March 1996ECETOC (1995A): Joint Assessment of Commodity Chemicals, Methacrylic Acid, CAS No
    N port O N N COMMISSIO 837 E INT RESEARCH CENTRE lic acid OH 3 EINECS No: 201-204-4 EUR 19 EUROPEA JO y CH methacr C 2 H CAS No: 79-41-4 European Union Risk Assessment Re Protection 25 : Substances Priority List st European Institute for Health and Consumer 1 Bureau Chemicals Existing Volume European Chemicals Bureau European Union Risk Assessment Report CAS: 79-41-4 EC: 201-204-4 methacrylic acid 25 PL-1 European Union Risk Assessment Report METHACRYLIC ACID CAS No: 79-41-4 EINECS No: 201-204-4 RISK ASSESSMENT LEGAL NOTICE Neither the European Commission nor any person acting on behalf of the Commission is responsible for the use which might be made of the following information 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, 2002 ISBN 92-894-1273-9 © European Communities, 2002 Reproduction is authorised provided the source is acknowledged. Printed in Italy METHACRYLIC ACID CAS No: 79-41-4 EINECS No: 201-204-4 RISK ASSESSMENT Final Report, 2002 Germany The risk assessment of methacrylic acid (MAA) has been prepared by Germany on behalf of the European Union. Contact point: Bundesanstalt für Arbeitsschutz und Arbeitsmedizin Anmeldestelle Chemikaliengesetz (BAuA) (Federal Institute for Occupational Safety and Health Notification Unit) Friedrich-Henkel-Weg 1-25 44149 Dortmund Germany Fax: +49 (231) 9071-679 e-mail: [email protected] Date of Last Literature Search: 1995 Review of report by MS Technical Experts finalised: 1999 Final report: 2002 (The last full literature survey was carried out in 1995 - targeted searches (for example on grouting) were carried out subsequently, and information found through scanning certain sources has also been included).
    [Show full text]
  • Methycryolic Acid and Esters, Supp. A
    Report No. 11 A METHACRYLIC ACID METHACRYLIC ESTERS Supplement A by DONALD C. THOMAS Contributions by Brij M. Sood and Leslie A. Carmichael May 1974 A private report by the PROCESS ECONOMICS PROGRAM I STANFORD RESEARCH INSTITUTE MENLO PARK, CALIFORNIA I - - CONTENTS 1 INTRODUCTION . 1 2 SUMMARY................,.......... 3 Methyl Methacrylate via Acetone Cyanohydrin . 5 Methyl Methacrylate from Isobutylene via Methacrylonitrile . 6 Methyl Methacrylate from Isobutylene via Methacrylic Acid . 7 3 COMPARISON OF PROCESSES . 9 4 INDUSTRY STATUS . 15 5 METHYL METHACRYLATE VIA ACETONE CYANOHYDRIN ......... 19 Review of Processes ..................... 19 Hydrogen Cyanide Production ................ 19 Acetone Cyanohydrin Production .............. 21 Hydrolysis and Esterification ............... 24 Recovery of Methyl Methacrylate .............. 25 Handling and Disposition of Ammonium Bisulfate ...... 26 Process Description ..................... 29 Hydrogen Cyanide Production ................ 29 Acetone Cyanohydrin Production .............. 32 Hydrolysis and Esterification ............... 33 Purification ....................... 34 Sulfuric Acid Regeneration ................ 34 Process Discussion ..................... 49 Waste Treatment ....................... 50 Cost Estimates ....................... 52 6 METHYL METHACRYLATE FROM ISOBUTYLENE VIA METHACRYLONITRILE ...................... 61 Review of Processes ..................... 61 Methacrylonitrile Production ............... 61 Treatment of Ammoxidation By-Products ........... 65 Hydrolysis and
    [Show full text]
  • Toxicological Review of Methyl Methacrylate
    TOXICOLOGICAL REVIEW of METHYL METHACRYLATE (CAS No. 80-62-6) In Support of Summary Information on the Integrated Risk Information System (IRIS) January 1998 U.S. Environmental Protection Agency Washington, DC TABLE OF CONTENTS DISCLAIMER ............................................................ i FOREWORD ............................................................ ii CONTRIBUTORS AND REVIEWERS ........................................ iii 1. INTRODUCTION ....................................................... 1 2. CHEMICAL AND PHYSICAL INFORMATION RELEVANT TO ASSESSMENTS . 2 3. TOXICOKINETICS/TOXICODYNAMICS RELEVANT TO ASSESSMENTS ........ 4 3.1. ABSORPTION ...................................................... 4 3.2. DISTRIBUTION .................................................... 4 3.3. METABOLISM ..................................................... 6 3.4. EXCRETION ...................................................... 8 4. HAZARD IDENTIFICATION ............................................. 10 4.1. STUDIES IN HUMANS ............................................. 10 4.1.1. Human Noncancer Studies ....................................... 10 4.1.2. Human Cancer Studies .......................................... 15 4.2. PRECHRONIC, CHRONIC, AND CANCER BIOASSAYS IN ANIMALS ...... 16 4.2.1. Acute Inhalation Studies ......................................... 16 4.2.2. Subchronic and Chronic Inhalation Studies ........................... 19 4.2.3. Acute Oral Studies ............................................. 26 4.2.4. Subchronic and
    [Show full text]
  • Properties and Interactions of Oral Structures and Restorative Materials
    1 NBSIR 80-2168 Properties and Interactions of Oral Structures and Restorative Materials James M. Cassel, J. A. Tesk, G. M. Brauer, J. M. Antonucci, W. Wu, J. E. McKinney, R. P. Whitlock, and R. Hinman Dental and Medical Materials Polymer Science and Standards Division Center for Materials Science National Measurement Laboratory National Bureau of Standards Washington, DC 20234 Annual Report for Period October 1, 1979 thru September 30, 1980 November 1980 Interagency Agreement YOI-DE-4001 5-1 — r ed for QO nal Institute of Dental Research 100 isda, MD 20014 . U56 80-2163 1980 Ci 2 I 1 . national bureau of standards NBSIR 80-2168 LIBRARY AUG 7 1981 PROPERTIES AND INTERACTIONS OF not dec - c; rc ORAL STRUCTURES AND RESTORATIVE CXcfdo MATERIALS no- %0'c5/6# James M. Cassel, J. A. Tesk, G. M. Brauer, J. M. Antonucci, W. Wu, J. E. McKinney, R. P. Whitlock, and R. Hinman mo Dental and Medical Materials Polymer Science and Standards Division Center for Materials Science National Measurement Laboratory National Bureau of Standards Washington, DC 20234 Annual Report for Period October 1, 1979 thru September 30, 1980 November 1980 Interagency Agreement YOI-DE-4001 5-1 Certain commercial materials and equipment are identified in this report to specify the experimental procedure. In no instance does such identification imply recommendation or endorsement by the National Bureau of Standards or that the materials and equipment identified are necessarily the best available for the purpose. Prepared for National Institute of Dental Research Bethesda, MD 20014 U S. DEPARTMENT OF COMMERCE, Philip M. Klutznick, Secretary Luther H.
    [Show full text]
  • Selective Oxidation of Isobutane to Methacrylic Acid and Methacrolein: a Critical Review
    catalysts Review Selective Oxidation of Isobutane to Methacrylic Acid and Methacrolein: A Critical Review Li Zhang ,Sébastien Paul , Franck Dumeignil * and Benjamin Katryniok * University Lille, CNRS, Centrale Lille, University Artois, UMR 8181–UCCS–Unité de Catalyse et Chimie du Solide, F-59000 Lille, France; [email protected] (L.Z.); [email protected] (S.P.) * Correspondence: [email protected] (F.D.); [email protected] (B.K.) Abstract: Selective oxidation of isobutane to methacrolein (MAC) and methacrylic acid (MAA) has received great interest both in the chemical industry and in academic research. The advantages of this reaction originate not only from the low cost of the starting material and reduced process complexity, but also from limiting the use of toxic reactants and the production of wastes. Successive studies and reports have shown that heteropolycompounds (HPCs) with Keggin structure (under the form of partially neutralized acids with increased stability) can selectively convert isobutane to MAA and MAC due to their strong and tunable acidity and redox properties. This review hence aims to discuss the Keggin-type HPCs that have been used in recent years to catalyze the oxidation of isobutane to MAA and MAC, and to review alternative metal oxides with proper redox properties for the same reaction. In addition, the influence of the main reaction conditions will be discussed. Keywords: Keggin-type HPCs; isobutane; oxidation; methacrolein; methacrylic acid Citation: Zhang, L.; Paul, S.; 1. Introduction Dumeignil, F.; Katryniok, B. Selective Hydrocarbons are generally issued from coal, oil, and natural gas. They are still the Oxidation of Isobutane to Methacrylic main feedstock of the chemical industry.
    [Show full text]
  • Mechanism of the Hydroxyl Radical Oxidation of Methacryloyl Peroxynitrate (Mpan) and Its Pathway Toward Secondary Organic Aerosol Formation in the Atmosphere
    335 Appendix C MECHANISM OF THE HYDROXYL RADICAL OXIDATION OF METHACRYLOYL PEROXYNITRATE (MPAN) AND ITS PATHWAY TOWARD SECONDARY ORGANIC AEROSOL FORMATION IN THE ATMOSPHERE Nguyen, T. B., K. H. Bates, J. D. Crounse, R. H. Schwantes, X. Zhang, H. G. Kjaergaard, J. D. Surratt, P. Lin, A. Laskin, J. H. Seinfeld, and P. O. Wennberg (2015). “Mechanism of the hydroxyl radical oxidation of methacryloyl perox- ynitrate (MPAN) and its pathway toward secondary organic aerosol formation in the atmosphere”. In: Phys. Chem. Chem. Phys. 17.27, pp. 17914–17926. : 10.1039/C5CP02001H. Abstract Methacryloyl peroxynitrate (MPAN), the acyl peroxynitrate of methacrolein, has been suggested to be an important secondary organic aerosol (SOA) precursor from isoprene oxidation, but the mechanism by which MPAN produces SOA through re- action with the hydroxyl radical (OH) remains unclear. We systematically evaluate three proposed mechanisms in controlled chamber experiments and provide the first experimental support for the theoretically-predicted lactone formation pathway from the MPAN + OH reaction, producing hydroxymethyl-methyl-↵-lactone (HMML). The decomposition of the MPAN-OH adduct yields HMML + NO ( 75%) and 3 ⇠ hydroxyacetone + CO + NO ( 25%), out-competing its reaction with atmospheric 3 ⇠ oxygen. The production of other proposed SOA precursors, e.g. methacrylic acid epoxide (MAE), from MPAN and methacrolein are negligible (<2%). Furthermore, we show that the β-alkenyl moiety of MPAN is critical for lactone formation. Alkyl radicals formed cold via H-abstraction by OH do not decompose to HMML, even if they are structurally identical to the MPAN-OH adduct. The SOA formation from HMML, from polyaddition of the lactone to organic compounds at the particle in- terface or in the condensed phase, is close to unity under dry conditions.
    [Show full text]
  • Methacrylic Acid and Methacrylic Esters
    PROCESS ECONOMICS PROGRAM ..-. SRI INTERNATIONAL Mm10 Park, California Abstract 9402E Process Economics Program Report No. 11C METHACRYLIC ACID AND METHACRYLIC ESTERS (September 1984) For the last fifteen years, processes have been developed to supplant the established process for making methyl methacrylate from acetone, hydrogen cyanide, and methanol. The acetone cyanohydrin route suffers from production of acidic wastes; the newer processes avoid these wastes and offer lower costs. Since our most recent previous report on the subject (Report LlB, issued in July 1980), a methyl methacrylate process based on a C4 feed- stock has been commercialized in Japan. This process oxidizes a t-butanol feed to methacrolein and methacrylic acid in two stages, then esterifies the acid to methyl methacrylate. We have evaluated this process and several variations, including the alternative use of isobutane feed and the supplementary use of isobutyraldehyde (by-product from 0x0 alcohol plants). We have also evaluated an attractive process based on propylene hydrocarboxylation to isobutyric acid, followed by dehydrogenation to methacrylic acid. We have updated some of the processes evaluated in Report llB, including the acetone cyanohydrin process. For a newly constructed plant, and at market prices for HCN and acetone, the acetone cyanohydrin process is more expensive than several of the newer processes. PEP'83 RHS - ReportNo. 11C a METHACRYLIC ACID AND ESTERS SUPPLEMENT C by ROBERT H. SCHWAAR ETSUO MATSUNAGA SHOICHI KIKUCHI a- and WATARU NISHIMOTO September 1984 - Cl a A private report by the PROCESS ECONOMICS PROGRAM a m Menlo Park, California 94025 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research.
    [Show full text]
  • Methoxy Poly (Ethylene Glycol) Methacrylate - Based
    METHOXY POLY (ETHYLENE GLYCOL) METHACRYLATE - BASED COPOLYMERS ON THE APPLICATIONS OF CONCRETE ADMIXTURES, MESOPOROUS MATERIALS, AND RHEOLOGY MODIFIERS A Dissertation Presented to The Graduate Faculty of The University of Akron In Partial Fulfillment of the Requirements for the Degree Doctor of Philosophy Pattarasai Tangvijitsakul December, 2015 METHOXY POLY (ETHYLENE GLYCOL) METHACRYLATE - BASED COPOLYMERS ON THE APPLICATIONS OF CONCRETE ADMIXTURES, MESOPOROUS MATERIALS, AND RHEOLOGY MODIFIERS Pattarasai Tangvijitsakul Dissertation Approved: Accepted: Advisor Department Chair Dr. Mark D. Soucek Dr. Sadhan C. Jana Committee Chair Dean of the College Dr. Kevin Cavicchi Dr. Eric J. Amis Committee Member Interim Dean of the Graduate School Dr. Avraam I. Isayev Dr. Chand Midha Committee Member Date Dr. Li Jia Committee Member Dr. Chrys Wesdemiotis ii ABSTRACT Hydrophilic copolymers were prepared and used in different applications including dispersant additives for cement, thin film batteries, and thickener in water- borne latex coating respectively. The copolymers were prepared using methoxy [poly (ethylene glycol) methacrylate] or MPEGMA and methacrylic acid (MAA) by different polymerization techniques e.g. reversible addition-fragmentation chain transfer (RAFT) polymerization, conventional radical polymerization, and esterification process. Different ratios of monomers and different side chain lengths of MPEGMA were utilized in order to investigate those effects of the fluidity of fresh cement/concrete. The effect molecular weight, molecular weight distribution, and the copolymer structures on fluidity of fresh cement/concrete were also studied. In addition, it was found that a new RAFT polycarboxylate terpolymer (containing in-situ defoaming groups) not only able to provide a reasonable cement fluidity over a long period of time, but also able to control the amount of generated bubbles at the same time.
    [Show full text]