Butoxymethyl)- (N-Butyl Glycidyl Ether
Total Page:16
File Type:pdf, Size:1020Kb
Load more
Recommended publications
-
The Utilization of Ti-SBA-15 Catalyst in the Epoxidation of Allylic Alcohols
Reac Kinet Mech Cat (2012) 105:451–468 DOI 10.1007/s11144-011-0405-1 The utilization of Ti-SBA-15 catalyst in the epoxidation of allylic alcohols Agnieszka Wro´blewska • Edyta Makuch Received: 17 August 2011 / Accepted: 16 November 2011 / Published online: 2 December 2011 Ó The Author(s) 2011. This article is published with open access at Springerlink.com Abstract Ti-SBA-15, one of the latest titanium silicalite catalysts, has been pre- pared according to the literature by the direct hydrothermal synthesis using Pluronic 123 as structure-directing agent. The characterization of the catalyst was performed by means of the following methods: XRD, IR, UV–Vis, X-ray microanalysis and SEM. The catalytic properties of the Ti-SBA-15 catalyst have been tested in the epoxidation of allyl alcohol, methallyl alcohol, crotyl alcohol and 1-butene-3-ol with hydrogen peroxide. The process has been described by the following main functions: the selectivity to epoxide compound in relation to allylic compound consumed and the conversion of allylic compound. Keywords Ti-SBA-15 Á Allylic compounds Á Epoxide compounds Á Liquid-phase epoxidation Á Hydrogen peroxide Mathematics Subject Classification (2000) 32 Á 46 Á 92 JEL Classification I23 Á L65 Introduction Zeolites with titanium atoms in the structure have wide applications in oxidation processes (especially in epoxidation processes) which are carried out in the presence of hydrogen peroxide (oxidizing agent). To the group of these zeolites belong TS-1 and TS-2 catalysts—the first titanium silicalite catalysts [1, 2]. TS-1 and TS-2 are microporous materials with relatively small pore size (about 0.5 nm), which limits A. -
A New Approach to Prepare Polyethylene Glycol Allyl Glycidyl Ether
E3S Web of Conferences 267, 02004 (2021) https://doi.org/10.1051/e3sconf/202126702004 ICESCE 2021 A new approach to prepare Polyethylene Glycol Allyl Glycidyl Ether Huizhen Wang1*, Ruiyang Xie1, Mingjun Chen1*, Weihao Deng1, Kaixin Zhang2, Jiaqin Liu1 1School of Science, Xihua University, Chengdu 610039, China; 2Chengdu Jingyiqiang Environmental Protection Technology Co., Ltd. Abstract. The polyethylene glycol allyl glycidyl ether (PGAGE) is an important intermediate for preparing silicone softener that can be synthesized from allyl alcohol polyoxyethylene ether and epichlorohydrin (ECH). The performance parameters including the concentration of ECH, initial boron trifluoride diethyl etherate (BFEE) as well as CaCl2 quality were investigated respectively. The optimum process parameters which can get high capping and low by-product rate are as follows: the ECH concentration is 2.0 M, the initial BFEE concentration is 1.65mM, and the CaCl2 dosage is 1.65g/L. Under these conditions, the maximal yield can be improved to 91.36%, the percent of capping rate is higher than 98.16%, the residual concentration of F- is only 0.63 mg/L. concentrated basic solution, in which the total yield was between 90%~91% by Matsuoka et al. [10] also use the 1 Introduction two-step reaction to synthesize AGE based on the reaction Polyethylene glycol allyl glycidyl ether (PGAGE) and the of allyl alcohol with ECH using BFEE as the catalyst. allyl polyoxyethylene ether (APEG), tethering with both Their results demonstrated that the yield reaches 82% alkene and epoxy groups, are widely used as fabric under the following condition: n (ECH) : n (allyl alcohol): finishing agent [1-2] , reactive diluent [3] , cross-linking (catalysis) = 1: (1~3) : (0.01~0.002). -
A New Coupling Process for Synthesis of Epichlorohydrin from Dichloropropanols
2nd International Conference on Machinery, Materials Engineering, Chemical Engineering and Biotechnology (MMECEB 2015) A new coupling process for synthesis of epichlorohydrin from dichloropropanols Dawei Wu, Sumin Zhou* School of Chemical Engineering, Huaiyin Institute of Technology, Huaian 223005, China [email protected] Keywords: dichloropropanol, epichlorohydrin, tubular reactor, wiped film evaporation. Abstract. As an important material used in the production of epoxy resins, epichlorohydrin is usually derived from the saponification and cyclization of dichloropropanol in a tower reacting system. In order to reduce energy consumption and wastewater discharge, a new process of tubular reactor coupled with wiped film evaporation was adopt to produce epichlorohydrin. The effects of different technological parameters on the yield of the coupling process were investigated, such as reactants' molar ratio, reaction & evaporation temperature, residence time and so on. Results indicated that the use of coupling process will significantly reduce the material consumption and shorter the reaction time. This coupling process provided a useful suggestion for the design of the industrial plants. 1. Introduction Epichlorohydyin(ECH), also known as 1-chloro-2, 3-epoxy propane, is an important chemical material, mainly used to synthesizing epoxy resin, chlorohydrins rubber, pesticide, plasticizer and so on [1]. The main method to produce ECH is high-temperature chlorination of propylene [2]. With the fast-development of biodiesel production, the use of glycerol for producing ECH [3-4] is going to mature and has become an important industrial technological process [5]. Although the difference raw materials were used, the processes also consist of two reaction steps as well. First step is the saponification and cyclization of dichloropropanol (DCP) to produce ECH. -
Optimization of the Synthesis of Glycerol Derived Monoethers from Glycidol by Means of Heterogeneous Acid Catalysis
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Repositorio Universidad de Zaragoza molecules Article Optimization of the Synthesis of Glycerol Derived Monoethers from Glycidol by Means of Heterogeneous Acid Catalysis Elisabet Pires 1,2,* , José Ignacio García 1, Alejandro Leal-Duaso 1, José Antonio Mayoral 1,2, José Ignacio García-Peiro 2 and David Velázquez 2 1 Instituto de Síntesis Química y Catálisis Homogénea (ISQCH), CSIC-University of Zaragoza-Calle Pedro Cerbuna, 12, E-50009 Zaragoza, Spain; [email protected] (J.I.G.); [email protected] (A.L.-D.); [email protected] (J.A.M.) 2 Departmento de Química Orgánica, Facultad de Ciencias, University of Zaragoza, Calle Pedro Cerbuna, 12, E-50009 Zaragoza, Spain; [email protected] (J.I.G.-P.); [email protected] (D.V.) * Correspondence: [email protected]; Tel.: +34-876-553501 Received: 7 October 2018; Accepted: 3 November 2018; Published: 6 November 2018 Abstract: We present an efficient and green methodology for the synthesis of glycerol monoethers, starting from glycidol and different alcohols, by means of heterogeneous acid catalysis. A scope of Brønsted and Lewis acid catalysts were applied to the benchmark reaction of glycidol and methanol. The selected catalysts were cationic exchangers, such as Nafion NR50, Dowex 50WX2, Amberlyst 15 and K10-Montmorillonite, both in their protonic form and exchanged with Al(III), Zn(II) and Fe(III). Thus, total conversions were reached in short times by using 1 and 5% mol catalyst loading and room temperature, without the need for excess glycidol or the presence of a solvent. -
Production of Glycidyl Compounds
Office europeen des brevets (fi) Publication number : 0 491 529 A1 @ EUROPEAN PATENT APPLICATION @ Application number : 91311630.7 © Int. CI.5: C07D 301/28, C07D 303/24 (22) Date of filing : 13.12.91 (30) Priority : 18.12.90 GB 9027448 (72) Inventor : Thoseby, Michael Robert 29 De Freville Avenue Cambridge (GB) (43) Date of publication of application : Inventor : Rolfe, William Martin 24.06.92 Bulletin 92/26 42 Vetch Walk Haverhill, Suffolk (GB) (S) Designated Contracting States : CH DE ES FR GB IT LI NL (74) Representative : Sparrow, Kenneth D. et al CIBA-GEIGY PLC. Patent Department, Central Research, Hulley Road @ Applicant : CIBA-GEIGY AG Macclesfield, Cheshire SK10 2NX (GB) Klybeckstrasse 141 CH-4002 Basel (CH) (54) Production of glycidyl compounds. (57) A process for the production of a glycidyl ether of an alcohol, comprising reacting an alcohol with epichlorohydrin, in substantially the stoichiometric proportions required to pro- duce the 1:1 adduct, in the presence, as catal- yst, of a salt of perchloric acid or trifluoromethane sulphonic acid with a metal of Group IMA of the Periodic Table of Elements (according to the IUPAC 1970 convention) ; and then dehydrochlorinating the product so obtained. CM LU Jouve, 18, rue Saint-Denis, 75001 PARIS 1 EP 0 491 529 A1 2 The present invention relates to a process for the 100 parts by weight of the alcohol reactant. production of glycidyl compounds. The alcohol reactant may be a primary, secon- The addition reaction between epoxides and dary or tertiary alcohol. While monohydric alcohols alcohols, in the presence of a catalyst, to produce an may be used, e.g. -
Gasket Chemical Services Guide
Gasket Chemical Services Guide Revision: GSG-100 6490 Rev.(AA) • The information contained herein is general in nature and recommendations are valid only for Victaulic compounds. • Gasket compatibility is dependent upon a number of factors. Suitability for a particular application must be determined by a competent individual familiar with system-specific conditions. • Victaulic offers no warranties, expressed or implied, of a product in any application. Contact your Victaulic sales representative to ensure the best gasket is selected for a particular service. Failure to follow these instructions could cause system failure, resulting in serious personal injury and property damage. Rating Code Key 1 Most Applications 2 Limited Applications 3 Restricted Applications (Nitrile) (EPDM) Grade E (Silicone) GRADE L GRADE T GRADE A GRADE V GRADE O GRADE M (Neoprene) GRADE M2 --- Insufficient Data (White Nitrile) GRADE CHP-2 (Epichlorohydrin) (Fluoroelastomer) (Fluoroelastomer) (Halogenated Butyl) (Hydrogenated Nitrile) Chemical GRADE ST / H Abietic Acid --- --- --- --- --- --- --- --- --- --- Acetaldehyde 2 3 3 3 3 --- --- 2 --- 3 Acetamide 1 1 1 1 2 --- --- 2 --- 3 Acetanilide 1 3 3 3 1 --- --- 2 --- 3 Acetic Acid, 30% 1 2 2 2 1 --- 2 1 2 3 Acetic Acid, 5% 1 2 2 2 1 --- 2 1 1 3 Acetic Acid, Glacial 1 3 3 3 3 --- 3 2 3 3 Acetic Acid, Hot, High Pressure 3 3 3 3 3 --- 3 3 3 3 Acetic Anhydride 2 3 3 3 2 --- 3 3 --- 3 Acetoacetic Acid 1 3 3 3 1 --- --- 2 --- 3 Acetone 1 3 3 3 3 --- 3 3 3 3 Acetone Cyanohydrin 1 3 3 3 1 --- --- 2 --- 3 Acetonitrile 1 3 3 3 1 --- --- --- --- 3 Acetophenetidine 3 2 2 2 3 --- --- --- --- 1 Acetophenone 1 3 3 3 3 --- 3 3 --- 3 Acetotoluidide 3 2 2 2 3 --- --- --- --- 1 Acetyl Acetone 1 3 3 3 3 --- 3 3 --- 3 The data and recommendations presented are based upon the best information available resulting from a combination of Victaulic's field experience, laboratory testing and recommendations supplied by prime producers of basic copolymer materials. -
Filter Chart
Filter Chart Chemical Filter Chemical Filter Chemical Filter Abate FFP1 tert-Butyl acetate A1 Copper fume FFP1 Acetaldehyde A1 Butyl acrylate A1 Dusts & mist (as Cu) FFP1 Acetic acid E1 n-Butyl alcohol A1 Cotton dust, raw FFP1 Acetic anhydride B1 sec-Butyl alcohol R A1 Crag herbicide FFP1 Acetonitrile A1 Butylamine B1 Cresol, all isomers FFP1 Acetylene dichloride A1 tert-Butyl chromate (as Cro3) FFP1 Cumene FFP1 Acetylene tetrabromide A1 n-Butyl glycidyl ether(BGE) A1 Cyanamide A1 P1 Acetylsalicylic acid FFP2 n-Butyl lactate A1 Cyanogen B1 Acrolein A1 o-sec Butyl phenol A1 Acrylamide A1 P2 p-tert Butyltoluene A1 Cyanogen chloride (CK) B1 Acrylonitrile A1 Cadmium, dust & salts (as Cd) FFP1 Cyclohexane A1 Aldrin A1 P2 Cadmium oxide fume (as Cd) FFP1 Cyclohexnol A1 Allyl alcohol A1 Calcium cyanamide FFP1 Cyclohexanone A1 Allyl chloride A1 Calcium hydroxide FFP1 Cyclohexene Allyl glycidyl ether (AGE) A1 Calcium oxide FFP1 A1 Allyl propyl disulfide B1 Camphor, synthetic A1 Cyclohexylamine A1 Aluminium metal and oxide FFP2 Caprolactam Dust FFP1 Cyclonite B1 Aluminium pyro powders FFP2 Vapor A1 1.3 Cyclopentadiene A1 Aluminium welding fumes A1 P2 Captafol(DifolatanR) FFP1 2.4-D (2.4-Dichlorophenoxy acetic acid) FFP1 Aluminium soluble salts FFP2 Captan FFP1 Aluminium, alkyls A1 R Carbary (Seven ) FFP1 D.D.T. (Dichlorodiphenyl A1 P1 4-Aminodiphenyl FFP1 Carbofuran (FuradanR) FFP1 trichloroethane) A1 P1 2- Aminoethanol A1 Carbon black FFP1 DDVP Decaborane B1 P1 2- Aminopyridine K1 Carbon dusulfide B1 DemetonR B1 P1 Ammonia A1 Carbon tetrabromide -
Vulcanizable Epichlorohydrin Polymer Composition
Europaisches Patentamt J European Patent Office © Publication number: 0 657 499 A1 Office europeen des brevets EUROPEAN PATENT APPLICATION © Application number: 94119434.2 © int. Ci.6; C08K 13/02, //(C08K1 3/02,3:26, 5:45) @ Date of filing: 08.12.94 © Priority: 09.12.93 JP 308836/93 © Applicant: DAISO CO., LTD. 1 9.04.94 JP 801 76/94 1 0-8, Edobori 1 -chome Nishi-ku @ Date of publication of application: Osaka-shi 14.06.95 Bulletin 95/24 Osaka-fu (JP) © Designated Contracting States: @ Inventor: Tomoshige, Yoshihiro DE ES FR GB IT Yasuda-shukusha 2-507, 348-7 Tohda-cho Masuda-shi, Shimane-ken (JP) Inventor: Nishi, Yoshikazu 35-5, Ohshima 2-chome Amagasaka-shi, Hyogo-ken (JP) Inventor: Tanaka, Hidekazu 7-1-205, Mukonosato 2-chome Amagasaka-shi, Hyogo-ken (JP) Inventor: Ohnuki, Kohji 1-6-12, Nishitachibana-cho Amagasaki-shi, Hyogo-ken (JP) Inventor: Matoba, Yasuo 9-8-104, Kayandoh-cho Nishinomiya-shi, Hyogo-ken (JP) © Representative: VOSSIUS & PARTNER Siebertstrasse 4 D-81675 Munchen (DE) © Vulcanizable epichlorohydrin polymer composition. © A vulcanizable composition which contains (a) 100 parts by weight of an epichlorohydrin polymer; m CO (b) 0.1 to 10 parts by weight of a 2,3-dimercaptopyrazine derivative or a 2,3-dimercaptoquinoxaline derivative; and (c) 1 to 10 parts by weight of a hydrotalcite compound, has the high vulcanization rate and the excellent long time storage stability. Rank Xerox (UK) Business Services (3. 10/3.09/3.3.4) EP 0 657 499 A1 The present invention relates to a curable composition based on an epichlorohydrin polymer having excellent vulcanization properties and storage stability. -
The Selective Epoxidation of Allyl Alcohol to Glycidol
THE SELECTIVE EPOXIDATION OF ALLYL ALCOHOL TO GLYCIDOL A THESIS SUBMITTED FOR THE DEGREE OF DOCTOR OF PHILOSOPHY Luke Martin Harvey B. Eng. (Newcastle), B. Sci. (Newcastle) Department of Chemical Engineering The University of Newcastle, Australia November 2020 This research was supported by an Australian Government Research Training Program (RTP) Scholarship STATEMENT OF ORIGINALITY I hereby certify that the work embodied in the thesis is my own work, conducted under normal supervision. The thesis contains no material which has been accepted, or is being examined, for the award of any other degree or diploma in any university or other tertiary institution and, to the best of my knowledge and belief, contains no material previously published or written by another person, except where due reference has been made. I give consent to the final version of my thesis being made available worldwide when deposited in the University’s Digital Repository, subject to the provisions of the Copyright Act 1968 and any approved embargo. Luke Harvey 25 November 2020 I ACKNOWLEDGMENT OF AUTHORSHIP I hereby certify that the work embodied in this thesis contains published paper/s/scholarly work of which I am a joint author. I have included as part of the thesis a written declaration endorsed in writing by my supervisor, attesting to my contribution to the joint publication/s/scholarly work. By signing below I confirm that Luke Martin Harvey contributed the design of the experimental program, conducted experiments, data analysis and scientific writing to the paper/ publication entitled “Influence of impurities on the epoxidation of allyl alcohol to glycidol with hydrogen peroxide over titanium silicate TS-1” and contributed the epoxidation chemistry portion of the experimentation and scientific writing to the paper/ publication entitled “Enhancing allyl alcohol selectivity in the catalytic conversion of glycerol; influence of product distribution on the subsequent epoxidation step”. -
Alkaline-Based Catalysts for Glycerol Polymerization Reaction: a Review
Preprints (www.preprints.org) | NOT PEER-REVIEWED | Posted: 26 July 2020 doi:10.20944/preprints202007.0649.v1 Peer-reviewed version available at Catalysts 2020, 10, 1021; doi:10.3390/catal10091021 Review Alkaline-based catalysts for glycerol polymerization reaction: a review Negisa Ebadipour1, Sébastien Paul1, Benjamin Katryniok1 and Franck Dumeignil1,* 1 Univ. Lille, CNRS, Centrale Lille, Univ. Artois, UMR 8181 – UCCS – Unité de Catalyse et Chimie du Solide, F-59000 Lille, France; [email protected] (N.E.); [email protected] (S.P.); [email protected] (B.K.) * Correspondence: [email protected]; Tel.: +33-(0)3-20-43-45-38 Abstract: Polyglycerols (PGs) are biocompatible and highly functional polyols with a wide range of applications, such as emulsifiers, stabilizers, antimicrobial agents, in many industries including cosmetics, food, plastic and biomedical. The demand increase for biobased PGs encourages researchers to develop new catalytic systems for glycerol polymerization. This review focuses on alkaline homogeneous and heterogeneous catalysts. The performances of the alkaline catalysts are compared in terms of conversion and selectivity, and their respective advantages and disadvantages are commented. While homogeneous catalysts exhibit a high catalytic activity, they cannot be recycled and reused, whereas solid catalysts can be partially recycled. The key issue for heterogenous catalytic systems, which is unsolved so far, is linked to their instability due to partial dissolution in the reaction medium. Further, this paper also reviews the proposed mechanisms of glycerol polymerization over alkaline-based catalysts and discuss the various operating conditions with an impact on the performances. More particularly, temperature and amount of catalyst proved to have a significant influence on glycerol conversion and on its polymerization extent. -
Allyl Glycidyl Ether
ENEA0080 - ALLYL GLYCIDYL ETHER ALLYL GLYCIDYL ETHER Safety Data Sheet ENEA0080 Date of issue: 12/22/2016 Version: 1.0 SECTION 1: Identification 1.1. Product identifier Product name : ALLYL GLYCIDYL ETHER Product code : ENEA0080 Product form : Substance Physical state : Liquid Formula : C6H10O2 Synonyms : 2-(ALLYLOXYMETHYL)OXIRANE 1,2-EPOXY-3-ALLYLOXYPROPANE [(2-PROPENYLOXY)METHYL]OXIRANE 1-(2-PROPENYLOXY)-2,3-EPOXYPROPANE Chemical family : EPOXY COMPOUND 1.2. Recommended use of the chemical and restrictions on use Recommended use : Chemical intermediate For research and industrial use only 1.3. Details of the supplier of the safety data sheet GELEST, INC. 11 East Steel Road Morrisville, PA 19067 USA T 215-547-1015 - F 215-547-2484 - (M-F): 8:00 AM - 5:30 PM EST [email protected] - www.gelest.com 1.4. Emergency telephone number Emergency number : CHEMTREC: 1-800-424-9300 (USA); +1 703-527-3887 (International) SECTION 2: Hazard(s) identification 2.1. Classification of the substance or mixture GHS-US classification Flammable liquids Category 3 H226 Acute toxicity (oral) Category 4 H302 Acute toxicity (inhalation:vapor) Category 3 H331 Skin sensitization Category 1 H317 Germ cell mutagenicity Category 2 H341 Reproductive toxicity Category 2 H361 Specific target organ toxicity (single exposure) Category 3 H335 Hazardous to the aquatic environment - Acute Hazard Category 3 H402 Full text of H statements : see section 16 2.2. Label elements GHS-US labeling Hazard pictograms (GHS-US) : GHS02 GHS06 GHS07 GHS08 Signal word (GHS-US) : Danger Hazard -
Comparisons of Epoxy Technology for Protective Coatings and Linings In
ComparisonsComparisons ofof EpoxyEpoxy TechnologyTechnology forfor ProtectiveProtective CoatingsCoatings andand LiningsLinings inin WastewaterWastewater FacilitiesFacilities By John D. Durig, General Polymers, Cincinnati, Ohio, USA Aeration tank at a wastewater plant. Bis F epoxy resin with an aliphatic or a cycloaliphatic amine curing agent is appropriate. Editor’s Note: This article was first presented at SSPC (Photos courtesy of the author) 99, The Industrial Protective Coatings Conference and Exhibit, November 14-18, 1999, in Houston, TX, USA, and published in The Proceedings of the Seminars, SSPC 99-14, pp. 31-37. poxy technology and methods of curing and Epoxy Resin Technology E reacting with amine-based hardeners have There are three types of epoxy resins that find application continued to evolve since the first epoxy patents were is- in wastewater treatment facilities: bisphenol A, bisphenol sued in the 1930s. The possible reactions combined with F, and novolac resins. These resins all result from reac- wide-ranging formulation additives have resulted in a myri- tions of epichlorohydrin with phenolic compounds. The ad of products that can easily confuse decision makers type and number of phenolic groups determine both when it comes to product selection. Adding to the confu- physical and performance properties of the cured resin. sion is the wide range of environmental factors that must be considered when choosing a protective coating system. Bisphenol A Resin Structure This article will identify the primary differences be- Bisphenol A is a reaction product of phenol and acetone. tween three types of epoxies and four types of amine- Bisphenol A is reacted with epichlorohydrin to form based hardeners typically used in coatings for wastewater diglycidylether bisphenol A resin or DGEBA.