Gas-Phase Oligomerization of Propene Initiated by Benzene Radical Cation
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Reactions of Benzene & Its Derivatives
Organic Lecture Series ReactionsReactions ofof BenzeneBenzene && ItsIts DerivativesDerivatives Chapter 22 1 Organic Lecture Series Reactions of Benzene The most characteristic reaction of aromatic compounds is substitution at a ring carbon: Halogenation: FeCl3 H + Cl2 Cl + HCl Chlorobenzene Nitration: H2 SO4 HNO+ HNO3 2 + H2 O Nitrobenzene 2 Organic Lecture Series Reactions of Benzene Sulfonation: H 2 SO4 HSO+ SO3 3 H Benzenesulfonic acid Alkylation: AlX3 H + RX R + HX An alkylbenzene Acylation: O O AlX H + RCX 3 CR + HX An acylbenzene 3 Organic Lecture Series Carbon-Carbon Bond Formations: R RCl AlCl3 Arenes Alkylbenzenes 4 Organic Lecture Series Electrophilic Aromatic Substitution • Electrophilic aromatic substitution: a reaction in which a hydrogen atom of an aromatic ring is replaced by an electrophile H E + + + E + H • In this section: – several common types of electrophiles – how each is generated – the mechanism by which each replaces hydrogen 5 Organic Lecture Series EAS: General Mechanism • A general mechanism slow, rate + determining H Step 1: H + E+ E El e ctro - Resonance-stabilized phile cation intermediate + H fast Step 2: E + H+ E • Key question: What is the electrophile and how is it generated? 6 Organic Lecture Series + + 7 Organic Lecture Series Chlorination Step 1: formation of a chloronium ion Cl Cl + + - - Cl Cl+ Fe Cl Cl Cl Fe Cl Cl Fe Cl4 Cl Cl Chlorine Ferric chloride A molecular complex An ion pair (a Lewis (a Lewis with a positive charge containing a base) acid) on ch lorine ch loronium ion Step 2: attack of -
Summary of Gas Cylinder and Permeation Tube Standard Reference Materials Issued by the National Bureau of Standards
A111D3 TTbS?? o z C/J NBS SPECIAL PUBLICATION 260-108 o ^EAU U.S. DEPARTMENT OF COMMERCE/National Bureau of Standards Standard Reference Materials: Summary of Gas Cylinder and Permeation Tube Standard Reference Materials Issued by the National Bureau of Standards QC 100 U57 R. Mavrodineanu and T. E. Gills 260-108 1987 m he National Bureau of Standards' was established by an act of Congress on March 3, 1901. The Bureau's overall goal i s t0 strengthen and advance the nation's science and technology and facilitate their effective application for public benefit. To this end, the Bureau conducts research to assure international competitiveness and leadership of U.S. industry, science arid technology. NBS work involves development and transfer of measurements, standards and related science and technology, in support of continually improving U.S. productivity, product quality and reliability, innovation and underlying science and engineering. The Bureau's technical work is performed by the National Measurement Laboratory, the National Engineering Laboratory, the Institute for Computer Sciences and Technology, and the Institute for Materials Science and Engineering. The National Measurement Laboratory Provides the national system of physical and chemical measurement; • Basic Standards 2 coordinates the system with measurement systems of other nations and • Radiation Research furnishes essential services leading to accurate and uniform physical and • Chemical Physics chemical measurement throughout the Nation's scientific community, • Analytical Chemistry industry, and commerce; provides advisory and research services to other Government agencies; conducts physical and chemical research; develops, produces, and distributes Standard Reference Materials; provides calibration services; and manages the National Standard Reference Data System. -
BENZENE AS a LARVICIDE for SCREW WORMS1 the Larval Stage
BENZENE AS A LARVICIDE FOR SCREW WORMS1 By D. C. PARMAN Assistant Entomologist, Investigations of Insects Affecting the Health of Animals, Bureau of Entomology, United States Department of Agriculture INTRODUCTION The larval stage of CocMiomyia macellaria Fab., generally known amonff stock raisers in the Southwest as the screw worm, causes con- siderable loss to the livestock industry, estimated as high as $5,000,000 in some years. It has been apparent that the larvicides used to kill the worms are either toxic to the animal or at least in most cases detrimental to the healing of the wounds. This toxicity was at first attributed to the screw worm, but as many cases were ob- served where the animal was practically consumed by the larvae and still lived until the loss of olood or injury to some vital organ brought de^th, it was surmised that the treatments with larvicides were the cause of many deaths. During the summer of 1916 syste- matic work was begun to find a more efficient larvicide than the phenols and chloroform which were generally used. At first an attempt was made to add something to these larvicides to counteract the toxic properties. As this was not successful it was deemed best to look for a chemical that might be used with more satis- factory results. Several chemical groups were studied for possible larvicides. EXPERIMENTAL PROCEDURE All available chemicals with possible larvicidal value were selected for laboratory tests to determine whether they would kill the larvae of the screw-worm fly. The first tests were made by pouring the chemical on a number of larvae in a tube, or dusting on just enough to cover the larvae. -
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. -
Reactions of Aromatic Compounds Just Like an Alkene, Benzene Has Clouds of Electrons Above and Below Its Sigma Bond Framework
Reactions of Aromatic Compounds Just like an alkene, benzene has clouds of electrons above and below its sigma bond framework. Although the electrons are in a stable aromatic system, they are still available for reaction with strong electrophiles. This generates a carbocation which is resonance stabilized (but not aromatic). This cation is called a sigma complex because the electrophile is joined to the benzene ring through a new sigma bond. The sigma complex (also called an arenium ion) is not aromatic since it contains an sp3 carbon (which disrupts the required loop of p orbitals). Ch17 Reactions of Aromatic Compounds (landscape).docx Page1 The loss of aromaticity required to form the sigma complex explains the highly endothermic nature of the first step. (That is why we require strong electrophiles for reaction). The sigma complex wishes to regain its aromaticity, and it may do so by either a reversal of the first step (i.e. regenerate the starting material) or by loss of the proton on the sp3 carbon (leading to a substitution product). When a reaction proceeds this way, it is electrophilic aromatic substitution. There are a wide variety of electrophiles that can be introduced into a benzene ring in this way, and so electrophilic aromatic substitution is a very important method for the synthesis of substituted aromatic compounds. Ch17 Reactions of Aromatic Compounds (landscape).docx Page2 Bromination of Benzene Bromination follows the same general mechanism for the electrophilic aromatic substitution (EAS). Bromine itself is not electrophilic enough to react with benzene. But the addition of a strong Lewis acid (electron pair acceptor), such as FeBr3, catalyses the reaction, and leads to the substitution product. -
Formation of Nitrous Oxide
1461 No. 5069 DECEMBER 24. 1966 NATURE E-+ CCI. --->- ECC1 3 + Cl- Formation of Nitrous Oxide THE mechanism of formation of nitrous oxide from am The tightly bound .CCI3 group will not be removable in monium nitrate is attributable to the recognized thermal the normal biochemical reaction and the enzyme molecule dissociation of ammonium salts followed in this instance will be inactivated. by nitration of ammonia and decomposition of the ensuing This process of enzyme inactivation could, in principle, nitramide. The mechanism of this latter stage has been account for the toxicity of carbon tetrachloride and studied by various workers, notably by Marlies and La similar compounds and also of many insecticides. The Merl. Further, the decomposition of methyl nitramido postulated mechanism would also explain the observation to tho oxide and methyl alcohol is on record 2. by Butlerl3 that carbon tetrachloride is reduced in vivo As the nitration process, for example, of benzene, is to chloroform. Thus a proportion of .CCls radicals may commonly accompanied by some oxidation, the possibility react with sites other than the enzyme and abstract, of its OCClllTcnce in the preparation of nitrous oxide with for example, a hydrogen atom from a hydroxyl group or formation of nitrogen peroxide is not surprising and from a sulphydryl group. The latter exchange does technically well recognized. It has also recently been the appear to be possible from energy considerations. subject of public concern. D(RS-H) = 89 kcalJmole (ref. 14), .J. KENNER D(CI3G-H) = 91·4 kcalJmole (ref. 9) 41 Burlington Road, I have found that the activation energy of the electron Withington, capture reaction in chloroform vapour Manchester 20. -
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. -
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. -
Optimization Study on the Azeotropic Distillation Process for Isopropyl Alcohol Dehydration
Korean J. Chem. Eng., 23(1), 1-7 (2006) Optimization study on the azeotropic distillation process for isopropyl alcohol dehydration Jungho Cho and Jong-Ki Jeon*,† Department of Chemical Engineering, Dong Yang University, 1, Kyochon-dong, Poongki-eup, Youngju, Gyeongbuk 750-711, Korea *Department of Chemical Engineering, Kongju National University, 182, Shinkwan-dong, Gongju, Chungnam 314-701, Korea (Received 9 August 2005 • accepted 26 November 2005) Abstract−Modeling and optimization work was performed using benzene as an entrainer to obtain a nearly pure an- hydrous isopropyl alcohol product from dilute aqueous IPA mixture through an azeotropic distillation process. NRTL liquid activity coefficient model and PRO/II with PROVISION 6.01, a commercial process simulator, were used to simulate the overall azeotropic distillation process. We determined the total reboiler heat duties as an objective function and the concentration of IPA at concentrator top as a manipulated variable. As a result, 38.7 mole percent of IPA at concentrator top gave the optimum value that minimized the total reboiler heat duties of the three distillation columns. Key words: Azeotropic Distillation, Entrainer, NRTL Liquid Activity Coefficient Model, Simulation, Optimization INTRODUCTION using special distillation. One is to utilize an azeotropic distillation process using benzene or cyclohexane as an entrainer [Font et al., An anhydrous isopropyl alcohol (IPA) product with purity over 2003; Tao et al., 2003; Al-Amer, 2000; Fele et al., 2000] and the 99.9% by weight has been widely used as a raw material of paint other is an extractive distillation process using ethylene glycol as a or ink products and as a solvent in electronic and medicine indus- solvent [Ligero and Ravagnani, 2003; Pinto et al., 2000]. -
Ethene, Propene, Butene and Isoprene Emissions from a Ponderosa Pine Forest Measured by Relaxed Eddy Accumulation
Atmos. Chem. Phys., 17, 13417–13438, 2017 https://doi.org/10.5194/acp-17-13417-2017 © Author(s) 2017. This work is distributed under the Creative Commons Attribution 3.0 License. Ethene, propene, butene and isoprene emissions from a ponderosa pine forest measured by relaxed eddy accumulation Robert C. Rhew1, Malte Julian Deventer1,*, Andrew A. Turnipseed2,*, Carsten Warneke3,4, John Ortega5, Steve Shen1, Luis Martinez6, Abigail Koss3,4, Brian M. Lerner3,4,a, Jessica B. Gilman3,4, James N. Smith5,b, Alex B. Guenther7, and Joost A. de Gouw3 1Department of Geography and Berkeley Atmospheric Sciences Center, University of California Berkeley, Berkeley, CA 94720-4740, USA 22B Technologies, Boulder CO 80301, USA 3Cooperative Institute for Research in Environmental Sciences (CIRES), University of Colorado Boulder, Boulder CO 80309, USA 4NOAA Earth System Research Laboratory, Boulder, CO 80305, USA 5Atmospheric Chemistry Observations and Modeling (ACOM), National Center for Atmospheric Research, Boulder, CO 80301, USA 6Ernest F. Hollings Undergraduate Scholarship program, NOAA, Boulder, CO 80305, USA 7Department of Earth System Science, University of California Irvine, Irvine, CA 92697-3100, USA anow at: Aerodyne Research Inc., Billerica, MA 01821-3976, USA bnow at: Department of Chemistry, University of California Irvine, Irvine, CA 92697-2025, USA *These authors contributed equally to this work. Correspondence to: Robert C. Rhew ([email protected]) Received: 21 April 2017 – Discussion started: 4 May 2017 Revised: 9 September 2017 – Accepted: 28 September 2017 – Published: 10 November 2017 Abstract. Alkenes are reactive hydrocarbons that influence tober flux, based on measurements and modeling, averaged local and regional atmospheric chemistry by playing impor- 62, 52, 24 and 18 µg m−2 h−1 for ethene, propene, butene tant roles in the photochemical production of tropospheric and isoprene, respectively. -
SDS # : 001046 Supplier's Details : Airgas USA, LLC and Its Affiliates 259 North Radnor-Chester Road Suite 100 Radnor, PA 19087-5283 1-610-687-5253
SAFETY DATA SHEET Propylene Section 1. Identification GHS product identifier : Propylene Chemical name : Propylene Other means of : propylene; 1-Propene; propylene in gaseous state, impure; propylene liquefied, impure; identification propene, pure; propylene, pure; Methylethene; Methylethylene; prop-1-ene; 1-Propylene; R 1270 Product type : Gas. Product use : Synthetic/Analytical chemistry. Synonym : propylene; 1-Propene; propylene in gaseous state, impure; propylene liquefied, impure; propene, pure; propylene, pure; Methylethene; Methylethylene; prop-1-ene; 1-Propylene; R 1270 SDS # : 001046 Supplier's details : Airgas USA, LLC and its affiliates 259 North Radnor-Chester Road Suite 100 Radnor, PA 19087-5283 1-610-687-5253 24-hour telephone : 1-866-734-3438 Section 2. Hazards identification OSHA/HCS status : This material is considered hazardous by the OSHA Hazard Communication Standard (29 CFR 1910.1200). Classification of the : FLAMMABLE GASES - Category 1 substance or mixture GASES UNDER PRESSURE - Liquefied gas GHS label elements Hazard pictograms : Signal word : Danger Hazard statements : Extremely flammable gas. Contains gas under pressure; may explode if heated. May displace oxygen and cause rapid suffocation. May form explosive mixtures with air. Precautionary statements General : Read and follow all Safety Data Sheets (SDS’S) before use. Read label before use. Keep out of reach of children. If medical advice is needed, have product container or label at hand. Close valve after each use and when empty. Use equipment rated for cylinder pressure. Do not open valve until connected to equipment prepared for use. Use a back flow preventative device in the piping. Use only equipment of compatible materials of construction. Always keep container in upright position.