Current Chemistry Letters Synthesis of Allyl-Glycidyl Ether by The
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Alcohols Combined 1405
ALCOHOLS COMBINED 1405 Formulas: Table 1 MW: Table 1 CAS: Table 2 RTECS: Table 2 METHOD: 1405, Issue 1 EVALUATION: PARTIAL Issue 1: 15 March 2003 OSHA : Table 2 PROPERTIES: Table 1 NIOSH: Table 2 ACGIH: Table 2 COMPOUNDS: (1) n-butyl alcohol (4) n-propyl alcohol (7) cyclohexanol (2) sec-butyl alcohol (5) allyl alcohol (8) isoamyl alcohol (3) isobutyl alcohol (6) diacetone alcohol (9) methyl isobutyl carbinol SYNONYMS: See Table 3. SAMPLING MEASUREMENT SAMPLER: SOLID SORBENT TUBE TECHNIQUE: GAS CHROMATOGRAPHY, FID (Coconut shell charcoal, 100 mg/50 mg) ANALYTE: Compounds above FLOW RATE: 0.01 to 0.2 L/min DESORPTION: 1 mL 5% 2-propanol in CS2 Compounds: (1-3 ) (4-9) VOL-MIN: 2 L 1 L INJECTION -MAX: 10 L 10 L VOLUME: 1 µL SHIPMENT: Routine TEMPERATURE -INJECTION: 220 °C SAMPLE -DETECTOR: 250 - 300 °C STABILITY: See Evaluation of Method. -COLUMN: 35 °C (7 minutes), to 60 °C at 5 °C/minute, hold 5 minutes, up to BLANKS: 2 to 10 field blanks per set 120 °C at 10 °C /minute, hold 3 minutes. CARRIER GAS: He, 4 mL/min ACCURACY COLUMN: Capillary, fused silica, 30 m x 0.32-mm RANGE STUDIED: Not studied [1, 2]. ID; 0.5 µm film polyethylene glycol, DB- wax or equivalent BIAS: Not determined CALIBRATION: Solutions of analyte in eluent (internal OVERALL standard optional) PRECISION (Ö ): Not determined rT RANGE: See EVALUATION OF METHOD. ACCURACY: Not determined ESTIMATED LOD: 1 µg each analyte per sample PRECISION: See EVALUATION OF METHOD. APPLICABILITY: This method may be used to determine two or more of the specified analytes simultaneously. -
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. -
Chapter 13.Pptx
Chapter 13: Alcohols and Phenols 13.1 Structure and Properties of Alcohols C C Alkanes Carbon - Carbon Multiple Bonds Carbon-heteroatom single bonds basic O C C C N C N C X O nitro alkane X= F, Cl, Br, I amines Alkenes Alkyl Halide Chapter 23 OH C C H O C O C C O C C Alkynes phenol alcohols ethers epoxide acidic Chapter 14 H H H C S C C C C S S C C S C C H C C sulfides thiols disulfide H H (thioethers) Arenes 253 Nomenclature of alcohols 1. In general, alcohols are named in the same manner as alkanes; replace the -ane suffix for alkanes with an -ol for alcohols CH3CH2CH2CH3 CH3CH2CH2CH2OH OH butane 1-butanol 2-butanol butan-1-ol butan-2-ol 2. Number the carbon chain so that the hydroxyl group gets the lowest number 3. Number the substituents and write the name listing the substituents in alphabetical order. Many alcohols are named using non-systematic nomenclature H C OH 3 OH OH C OH OH HO OH H3C HO H3C benzyl alcohol allyl alcohol tert-butyl alcohol ethylene glycol glycerol (phenylmethanol) (2-propen-1-ol) (2-methyl-2-propanol) (1,2-ethanediol) (1,2,3-propanetriol) 254 127 Alcohols are classified according to the H R C OH C OH H H degree of substitution of the carbon bearing H H 1° carbon the -OH group methanol primary alcohol primary (1°) : one alkyl substituent R R C OH C OH R R secondary (2°) : two alkyl substituents H R 2° carbon 3° carbon tertiary (3°) : three alkyl substituents secondary alcohol tertiary alcohol Physical properties of alcohols – the C-OH bond of alcohols has a significant dipole moment. -
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. -
Title Selective Reduction of Acrolein to Allyl Alcohol by a Vapor Phase
Selective Reduction of Acrolein to Allyl Alcohol by a Vapor Title Phase Hydrogen Transfer Reaction Author(s) Kunichika, Sango; Oka, Shinzaburo; Sakai, Mutsuji Bulletin of the Institute for Chemical Research, Kyoto Citation University (1966), 44(3): 215-220 Issue Date 1966-10-31 URL http://hdl.handle.net/2433/76125 Right Type Departmental Bulletin Paper Textversion publisher Kyoto University Selective Reduction of Acrolein to Allyl Alcohol by a Vapor Phase Hydrogen Transfer Reaction Sango KUNICHIKA,Shinzaburo OKA and Mutsuji SAKAI* (KunichikaLaboratory) (ReceivedJune 15, 1966) Selectivereduction of acroleinto ally! alcoholhas been achievedby a vapor phase hydrogen transferreaction using isopropyl alcohol as a hydrogendonor. It was foundthat the preferredcatalyst was 50 weight% zinc oxide-magnesiumoxide catalyst prepared by calcininga mixtureof zincnitrate and magnesiumoxide at 500°C. The optimumconditions were found to be as follows;reaction tem- perature,near 200°C,total feed rate, 45 moles/1.of catalyst/hr.,feed ratio of isopropylalcohol per acrolein,10 moles. Under theseconditions, the yieldsof allyl alcoholof 80-65% at 80-90% conversion of acroleinwere obtained. INTRODUCTION Acrolein has two reactive functional groups, one is carbonyl group and the other is carbon-carbon double bond. Selective reduction of acrolein to allyl alcohol has been studied by several investigators. The reaction was generally carried out by the following two methods: (1) the Meerwein-Ponndorf-Verley reduction1-3), (2) vapor phase hydrogen transfer reaction with various metal oxide catalysts using an alcohol as a hydrogen donor4-11> The liquid phase reaction has some technical difficulties owing to the polymeri- zation of acrolein especially at high conversion. Therefore, in the present work, the more promising vapor phase reaction has been studied to find an effective catalyst and favorable reaction conditions. -
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 -
Conversion of Glycerol Into Allyl Alcohol Over Potassium-Supported Zirconia-Iron Oxide Catalyst
Title Conversion of glycerol into allyl alcohol over potassium-supported zirconia-iron oxide catalyst Author(s) Konaka, Aya; Tago, Teruoki; Yoshikawa, Takuya; Nakamura, Ayaka; Masuda, Takao Applied catalysis b-environmental, 146, 267-273 Citation https://doi.org/10.1016/j.apcatb.2013.03.007 Issue Date 2014-03 Doc URL http://hdl.handle.net/2115/54715 Type article (author version) File Information Manuscript_Glycerol to Allyl Alcohol .pdf Instructions for use Hokkaido University Collection of Scholarly and Academic Papers : HUSCAP Conversion of Glycerol into Allyl Alcohol over Potassium-Supported Zirconia-Iron Oxide Catalyst Aya Konaka, Teruoki Tago*, Takuya Yoshikawa, Ayaka Nakamura, and Takao Masuda Research Group of Chemical Engineering, Division of Chemical Process Engineering, Faculty of Engineering, Hokkaido University, N13W8, Kita-ku, Sapporo, Hokkaido, Japan 060-8628 * Corresponding author should be addressed E-mail: [email protected] Tel: +81-11-706-6551 Fax: +81-11-706-6552 1 Abstract The catalytic conversion of glycerol was performed with iron oxide-based catalysts for production of allyl alcohol using a fixed-bed flow reactor at 623 K under atmospheric pressure. The glycerol dehydration proceeds on acid sites of catalysts while the allyl alcohol production is assumed to be catalyzed by non-acidic sites of catalysts through a hydrogen transfer mechanism. Different alkali metals, including Na, K, Rb, and Cs were supported on ZrO2-FeOX and all of them gave impressively higher allyl alcohol yield and suppressed glycerol dehydration due to the reduced catalyst acidic property. K-supported ZrO2-FeOX (K/ZrO2-FeOX) was chosen for further studies, and allyl alcohol yield remarkably increased up to 27 mol%-C at the K content of 3-5 mol%. -
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.