Provisional Peer-Reviewed Toxicity Values for Allyl Alcohol (Casrn 107-18-6)
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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. -
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). -
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. -
Removal of NO and SO2 by Pulsed Corona Discharge Process
Korean J. Chem. Eng., 18(3), 308-316 (2001) Removal of NO and SO2 by Pulsed Corona Discharge Process Young Sun Mok†, Ho Won Lee, Young Jin Hyun, Sung Won Ham*, Jae Hak Kim** and In-Sik Nam** Department of Chemical Engineering, Cheju National University, Ara, Cheju 690-756, Korea *Department of Chemical Engineering, Kyungil University, Hayang, Kyungbuk 712-701, Korea **Department of Chemical Engineering, Pohang University of Science & Technology, Pohang, Kyungbuk 790-784, Korea (Received 6 September 2000 • accepted 9 March 2001) − Abstract Overall examination was made on the removal of NO and SO2 by pulsed corona discharge process. The mechanism for the removal of NO was found to largely depend on the gas composition. In the absence of oxygen, most of the NO removed was reduced to N2; on the other hand, oxidation of NO to NO2 was dominant in the presence of oxygen even when the content was low. Water vapor was an important ingredient for the oxidation of NO2 to nitric acid rather than that of NO to NO2. The removal of NO only slightly increased with the concentration of ammonia while the effect of ammonia on the removal of SO2 was very significant. The energy density (power delivered/feed gas flow rate) can be a measure for the degree of removal of NO. Regardless of the applied voltage and the flow rate of the feed gas stream, the amount of NO removed was identical at the same energy density. The production of N2O increased with the pulse repetition rate, and the presence of NH3 and SO2 enhanced it. -
INF.20 Economic Commission for Europe Inland Transport Committee Definition Of
INF.20 Economic Commission for Europe Inland Transport Committee Working Party on the Transport of Dangerous Goods 6 March 2012 Joint Meeting of the RID Committee of Experts and the Working Party on the Transport of Dangerous Goods Bern, 19–23 March 2012 Item 5(a) of the provisional agenda Proposals for amendments to RID/ADR/ADN: pending issues Definition of LPG Transmitted by the Government of Switzerland We have observed contradictions in the definition of LPG adopted by the Joint Meeting at its Autumn 2010 session (ECE/TRANS/WP.15/AC.1/120, Annex II) as well as in the German translation we have discussed in Erfurt during the Conference of translation and edition of the German ADR. The actual definitions in each language are the following: ""Gaz de pétrole liquéfié (GPL)", un gaz liquéfié à faible pression contenant un ou plusieurs hydrocarbures légers qui sont affectés aux numéros ONU 1011, 1075, 1965, 1969 ou 1978 seulement et qui est principalement constitué de propane, de propène, de butane, des isomères du butane, de butène avec des traces d’autres gaz d’hydrocarbures. “‘Liquefied Petroleum Gas (LPG)’ means a low pressure liquefied gas composed of one or more light hydrocarbons which are assigned to UN Nos. 1011, 1075, 1965, 1969 or 1978 only and which consists mainly of propane, propene, butane, butane isomers, butene with traces of other hydrocarbon gases. „Flüssiggas (LPG)*: Unter geringem Druck verflüssigtes Gas, das aus einem oder mehreren leichten Kohlenwasserstoffen besteht, die nur der UN-Nummer 1011, 1075, 1965, 1969 oder 1978 zugeordnet sind und das hauptsächlich aus Propan, Propen, Butan, Butan-Isomeren und Buten mit Spuren anderer Kohlenwasserstoffgase besteht.“ One important point is different between French from one side and English and German from the other side, that is that in French the repetition of the “de” in the enumeration of possible gases brings to the conclusion that the main constituent of the LPG is one of the listed gases. -
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%. -
United States Patent (19) (11) Patent Number: 4,968,451 Scheibel Et Al
United States Patent (19) (11) Patent Number: 4,968,451 Scheibel et al. 45) Date of Patent: Nov. 6, 1990 (54) SOIL RELEASE AGENTS HAVING ALLYL-DERVED SULFONATED END CAPS FOREIGN PATENT DOCUMENTS 155710 9/1985 European Pat. Off. (75) Inventors: Jeffrey J. Scheibel; Eugene P. 180356 5/1986 European Pat. Off. Gosselink, both of Cincinnati, Ohio 1475798 6/1977 United Kingdom . (73) Assignee: The Procter & Gamble Company, OTHER PUBLICATIONS Cincinnati, Ohio S. C. Bright, C. E. Stubbs and L. Thompson, J. Appl. (21) Appl. No.: 474,709 Chem. Biotechnol, 1975, vol. 25, pp. 901-912. 22) Filed: Jan. 29, 1990 Norton et al., J. Org. Chem, vol. 33, No. 11, pp. 4158-4165 (1967). Related U.S. Application Data Primary Examiner-A. Lionel Clingman (63) Continuation of Ser. No. 237,598, Aug. 26, 1988, aban Attorney, Agent, or Firm-Leonard W. Lewis; Jerry J. doned. Yetter (51 Int, C. .................... CO7C 309/05; C08G 63/68; 57 ABSTRACT C11D 3/37 (52) U.S. C. ............................... 252/549; 252/174.19; The present invention relates to novel soil release 252/539; 252/558; 252/DIG. 15 agents, which are particular sulfonated linear tere (58) Field of Search ......................................... 252/549 phthalate ester oligomers (S.T.E. oligomers). The S.T.E. oligomers are especially suitable for formulation (56 References Cited into laundry products such as laundry detergents or U.S. PATENT DOCUMENTS fabric conditioners. Thus formulated, they provide ef. 3,821,169 6/1974 Duddey et al. ..................... 528/293 fective soil release treatments for fabrics laundered in 4,156,073 5/1979 Login ............. -
TOX-48: Allyl Acetate (CASRN 591-87-7), Allyl Alcohol (CASRN
National Toxicology Program Toxicity Report Series Number 48 NTP Technical Report on the Comparative Toxicity Studies of Allyl Acetate, Allyl Alcohol, and Acrolein (CAS Nos. 591-87-7, 107-18-6, and 107-02-8) Administered by Gavage to F344/N Rats and B6C3F1 Mice July 2006 National Institutes of Health Public Health Service U.S. Department of Health and Human Services FOREWORD The National Toxicology Program (NTP) is an interagency program within the Public Health Service (PHS) of the Department of Health and Human Services (HHS) and is headquartered at the National Institute of Environmental Health Sciences of the National Institutes of Health (NIEHS/NIH). Three agencies contribute resources to the program: NIEHS/NIH, the National Institute for Occupational Safety and Health of the Centers for Disease Control and Prevention (NIOSH/CDC), and the National Center for Toxicological Research of the Food and Drug Administration (NCTR/FDA). Established in 1978, the NTP is charged with coordinating toxicological testing activities, strengthening the science base in toxicology, developing and validating improved testing methods, and providing information about potentially toxic substances to health regulatory and research agencies, scientific and medical communities, and the public. The Toxicity Study Report series began in 1991. The studies described in the Toxicity Study Report series are designed and conducted to characterize and evaluate the toxicologic potential of selected substances in laboratory animals (usually two species, rats and mice). Substances selected for NTP toxicity studies are chosen primarily on the basis of human exposure, level of production, and chemical structure. The interpretive conclusions presented in the Toxicity Study Reports are based only on the results of these NTP studies. -
Plasma-Pd/Γ-Al203 Catalytic System for Methane, Toluene and Propene Oxidation: Effect of Temperature and Plasma Input Power
22nd International Symposium on Plasma Chemistry July 5-10, 2015; Antwerp, Belgium Plasma-Pd/γ-Al203 catalytic system for methane, toluene and propene oxidation: effect of temperature and plasma input power T. Pham Huu1, 2, P. Da Costa3, S. Loganathan1 and A. Khacef1 1 GREMI-UMR 6744, CNRS-Université d'Orléans, 14 rue d’Issoudun, P.O. Box 6744, FR-45067 Orléans Cedex 02, France 2 Institute of Applied Material Science, Vietnam Academy of Science and Technology, 1 Mac Dinh Chi, HCMC, Vietnam 3 Sorbonne Universités, UPMC Paris 6, Institut Jean Le Rond d’Alembert, CNRS UMR 7190, 2 place de la gare de ceinture, FR-78210 Saint Cyr l’école, France Abstract: A pulsed non-thermal plasma and 1 wt% Pd/γ-Al2O3 catalyst was used to investigate the CH4, C3H6, and C7H8 oxidation in air. Effects of temperature and specific input energy on the VOCs conversion were studied. The plasma-catalyst interaction revealed the benefit effect on the VOCs oxidation even at low temperature leading to high CO2 selectivity. The synergistic effect of combining plasma with catalyst in one-stage configuration is observed only for toluene. Keywords: non-thermal plasma, Pd/γ-Al203, synergistic effect, methane, propene, toluene, oxidation 1. Introduction 2. Experimental Volatile organic compounds (VOCs) emitted from The plasma reactor is a cylindrical DBD gives the various industrial and domestic processes are important possibility to combine the catalyst with plasma reactor in sources of air pollution and therefore, become a serious single stage (IPC) or two-stage (PPC) configuration as problem for damaging the human health and the shown in Fig. -
Selective Liquid-Phase Oxidation of Allyl Alcohol to Glycidol Over MWW Type Titanosilicalite
Reac Kinet Mech Cat (2011) 103:451–462 DOI 10.1007/s11144-011-0312-5 Selective liquid-phase oxidation of allyl alcohol to glycidol over MWW type titanosilicalite Anna Fajdek • Agnieszka Wro´blewska • Eugeniusz Milchert Received: 4 February 2011 / Accepted: 23 March 2011 / Published online: 7 April 2011 Ó The Author(s) 2011. This article is published with open access at Springerlink.com Abstract The results of the epoxidation of allyl alcohol with 30% hydrogen peroxide over the Ti-MWW catalyst have been presented. The studies were carried out under atmospheric pressure and in the presence of methanol as a solvent. The influence of the following technological parameters on the course of epoxidation was examined: temperature (20–60 °C), the molar ratio of AA/H2O2 (1:1–5:1), methanol concentration (5–90 wt%), catalyst content (0–5.0 wt%), reaction time (5–300 min) and intensity of stirring (0–500 rpm). Keywords Glycidol Á Ti-MWW catalyst Á Liquid-phase epoxidation Á Hydrogen peroxide Introduction Zeolites are crystalline aluminosilicates with 133 known frameworks. Their pores are highly monodisperse and have a fixed directionality within the crystal. The pores in these systems often have a character of cages and connection tubes. The uniformity of the channels in the zeolitic system means that they are extremely selective adsorbents for small molecules of particular geometries and sizes and so make highly selective catalytic supports and adsorbents. Due to the pore sizes comparable to the molecular dimensions, zeolites are also called molecular sieves [1]. MWW (MCM-22) is a molecular sieve which crystallizes as thin sheets or plates and has a unique and unusual crystal structure. -
Me2si(Benz[E]Indenyl)
Propene Polymerization Using Homogeneous MAO-Activated Metallocene Catalysts: Me2Si(Benz[e]lndenyI)2ZrClu'MAO vs. Me2Si(2-Me-Benz[e]lndenyI)2ZrClu'MAO STEPHAN JUNGLlNG,t ROLF MULHAUPT,b UDO STEHLlNG/ HANS-HERBERT BRINTZINGER/ DAVID FISCHER/ and FRANZ LANGHAUSER3 'Institut fOr Makromolekulare Chemie and Freiburger Materialforschungszentrum der Albert-Ludwigs-Universitat Freiburg, 0-79104 Freiburg, Germany; 2Fakultat fOr Chemie, Universitat Konstanz, 0-78434 Konstanz, Germany; and 3BASF AG Abteilung ZKP, 0-67056 Ludwigshafen, Germany SYNOPSIS Propene was polymerized at 40°C and 2-bar propene in toluene using methylalumoxane (MAO) activated rac-Me2Si(Benz[elIndenyl)2ZrCI2 (BI) and rac-Me2Si(2-Me Benz[elIndenyl)2ZrCl2 (MBI). Catalyst BI/MAO polymerizes propene with high activity to afford low molecular weight polypropylene, whereas MBI/MAO is less active and produces high molecular weight polypropylene. Variation of reaction conditions such as propene concentration, temperature, concentration of catalyst components, and addition of hydrogen reveals that the lower molecular weight polypropylene produced with BI/MAO results from chain transfer to propene monomer following a 2,1-insertion. A large fraction of both me tallocene catalyst systems is deactivated upon 2,1-insertion. Such dormant sites can be reactivated by H2-addition, which affords active metallocene hydrides. This effect of H2- addition is reflected by a decreasing content of head-to-head enchainment and the formation of polypropylene with n-butyl end groups. Both catalysts show a strong dependence of activity on propene concentration that indicates a formal reaction order of 1. 7 with respect to propene. MBI/MAO shows a much higher dependence of the activity on temperature than BI/MAO.