Polymerization of Propene and Butene with a Chiral Zirconocene and Methylalumoxane As Cocatalyst
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Butenes Separation, Supp. A
PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California 94025 Abstract Process Economics Program Report No. 71A BUTTLENES (October 1982) Demand is fast increasing for lsobutylene, especially that used in manufacturing methyl tertiary-butyl ether, and for high purity butene-1 to use as a copolymer in linear low density polyethylene. Because of their wide availability, mixed butane-butylene streams from oleflns plants and petroleum refineries are being increasingly fed to plants to separate butylenes for use in chemicals. This first supplement to Report No. 71 updates demand projections, production capacities, and separation techniques for high purity butene-1 and lsobutylene. The processes that are now available for separating and purifying both butene-1 and lsobutylene from mixed butyl- ene streams are evaluated and compared. Other procedures for obtaining butylenes, such as dehydrogenatlon, lsomerleatlon, and disproportion&ion, are not updated in this report. PEP’81 JLC Report No. 71A - BUTYLENES SUPPLEMENT A by JOHN L. CHADWICK I I October 1982 f-F0 0 A private report by the m PROCESS ECONOMICS PROGRAM 0 Menlo Park, California 94025 0 For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. The CHEMICALECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced in the United States and the WORLDPETROCHEMICALS Program covers major hkdrocarbons and their derivatives on a worldwide basis. In addition, the SRI DIRECTORYOF CHEMICALPRODUCERS services provide detailed lists of chemical producers by company, prod- uct, and plant for the United States and Western Europe. ii CONTENTS 1 INTRODUCTION . 1 2 SUMMARY . -
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. -
Supplement of Compilation and Evaluation of Gas Phase Diffusion Coefficients of Reactive Trace Gases in the Atmosphere
Supplement of Atmos. Chem. Phys., 15, 5585–5598, 2015 http://www.atmos-chem-phys.net/15/5585/2015/ doi:10.5194/acp-15-5585-2015-supplement © Author(s) 2015. CC Attribution 3.0 License. Supplement of Compilation and evaluation of gas phase diffusion coefficients of reactive trace gases in the atmosphere: Volume 2. Diffusivities of organic compounds, pressure-normalised mean free paths, and average Knudsen numbers for gas uptake calculations M. J. Tang et al. Correspondence to: M. J. Tang ([email protected]) and M. Kalberer ([email protected]) The copyright of individual parts of the supplement might differ from the CC-BY 3.0 licence. Table of Contents 1 Alkanes and cycloalkanes ............................................................................................ 1 1.1 CH 4 (methane), C 2H6 (ethane), and C 3H8 (propane) ............................................. 1 1.2 C 4H10 (butane, methyl propane) ............................................................................ 3 1.3 C 5H12 (n-pentane, methyl butane, dimethyl butane) ............................................. 5 1.4 C 6H14 (n-hexane, 2,3-dimethyl butane) ................................................................ 7 1.5 C 7H16 (n-heptane, 2,4-dimethyl pentane).............................................................. 9 1.6 C 8H18 (n-octane, 2,2,4-trimethyl pentane) .......................................................... 11 1.7 C 9H20 (n-nonane), C 10 H22 (n-decane, 2,3,3-trimethyl heptane) and C 12 H26 (n- dodecane) ................................................................................................................. -
Donor/Acceptor Metallocenes: a New Structure Principle in Catalyst Design
COMMUNICATIONS metal complex inside their tunnels, which makes these [19] C. Cascales, E. GutieÂrrez-Puebla, M. A. Monge, C. Ruiz-Valero, materials a good point of departure for designing new Angew. Chem. 1998, 110, 135 ± 138; Angew. Chem. Int. Ed. 1998, 37, 129 ± 131. catalysts; a stable framework after removal of the transition [20] H. Li, M. Eddaaoudi, D. A. Richardson, O. M. Yaghi, J. Am. Chem. metal complex; and large distances between the active metal Soc. 1998, 120, 8567. centers, which allows unhindered access of reactants to these [21] Hailian Li, O. M. Yaghi, J. Am. Chem. Soc. 1998, 120, 10569. centers through uniformly sized 8Rc channels. [22] T. E. Gier, X. Bu, P. Feng, G. D. Stucky, Nature 1998, 395, 154. [23] X. Bu, P. Feng, G. D. Stucky, J. Am. Chem. Soc. 1998, 120, 11204. [24] X. Bu, P. Feng, T. E. Gier, D. Zhao, G. D. Stucky, J. Am. Chem. Soc. 1998, 120, 13389. [25] H. Brumer, K. Wutz, New J. Chem. 1992, 16,57. Experimental Section [26] A. Corma, V. ForneÂs, S. B. Pergher, T. L. Maesennn, J. G. Buglass, Nature 1998, 396, 353. [27] SHELXTL, Siemens Energy & Automation Inc., Analytical Instru- X-ray structure analysis of ICMM-2Cu, ICMM-2Ag, and ICMM-2H: mentation, 1996. Orthorhombic, space group Pnna,MoKa, dimensions of crystals: 0.2 Â 0.1 Â 0.05, 0.02 Â 0.08 Â 0.2, and 0.04 Â 0.16 Â 0.2 mm, respectively; see Table 1 for the cell parameters. Data were collected in a Siemens SMART- CCD diffractometer using w scans over the range 3 < q < 268. -
Reactions of Alkenes and Alkynes
05 Reactions of Alkenes and Alkynes Polyethylene is the most widely used plastic, making up items such as packing foam, plastic bottles, and plastic utensils (top: © Jon Larson/iStockphoto; middle: GNL Media/Digital Vision/Getty Images, Inc.; bottom: © Lakhesis/iStockphoto). Inset: A model of ethylene. KEY QUESTIONS 5.1 What Are the Characteristic Reactions of Alkenes? 5.8 How Can Alkynes Be Reduced to Alkenes and 5.2 What Is a Reaction Mechanism? Alkanes? 5.3 What Are the Mechanisms of Electrophilic Additions HOW TO to Alkenes? 5.1 How to Draw Mechanisms 5.4 What Are Carbocation Rearrangements? 5.5 What Is Hydroboration–Oxidation of an Alkene? CHEMICAL CONNECTIONS 5.6 How Can an Alkene Be Reduced to an Alkane? 5A Catalytic Cracking and the Importance of Alkenes 5.7 How Can an Acetylide Anion Be Used to Create a New Carbon–Carbon Bond? IN THIS CHAPTER, we begin our systematic study of organic reactions and their mecha- nisms. Reaction mechanisms are step-by-step descriptions of how reactions proceed and are one of the most important unifying concepts in organic chemistry. We use the reactions of alkenes as the vehicle to introduce this concept. 129 130 CHAPTER 5 Reactions of Alkenes and Alkynes 5.1 What Are the Characteristic Reactions of Alkenes? The most characteristic reaction of alkenes is addition to the carbon–carbon double bond in such a way that the pi bond is broken and, in its place, sigma bonds are formed to two new atoms or groups of atoms. Several examples of reactions at the carbon–carbon double bond are shown in Table 5.1, along with the descriptive name(s) associated with each. -
University of Groningen Structural Characterization of a Cationic Zirconocene Olefin Polymerization Catalyst with Its Methylated
University of Groningen Structural characterization of a cationic zirconocene olefin polymerization catalyst with its methylated boralumoxane counterion Richter, Bodo; Meetsma, Auke; Hessen, Bart; Teuben, Jan H. Published in: Angewandte Chemie-International Edition in English IMPORTANT NOTE: You are advised to consult the publisher's version (publisher's PDF) if you wish to cite from it. Please check the document version below. Document Version Publisher's PDF, also known as Version of record Publication date: 2002 Link to publication in University of Groningen/UMCG research database Citation for published version (APA): Richter, B., Meetsma, A., Hessen, B., & Teuben, J. H. (2002). Structural characterization of a cationic zirconocene olefin polymerization catalyst with its methylated boralumoxane counterion. Angewandte Chemie-International Edition in English, 41(12), 2166 - 2169. Copyright Other than for strictly personal use, it is not permitted to download or to forward/distribute the text or part of it without the consent of the author(s) and/or copyright holder(s), unless the work is under an open content license (like Creative Commons). Take-down policy If you believe that this document breaches copyright please contact us providing details, and we will remove access to the work immediately and investigate your claim. Downloaded from the University of Groningen/UMCG research database (Pure): http://www.rug.nl/research/portal. For technical reasons the number of authors shown on this cover page is limited to 10 maximum. Download date: 10-02-2018 COMMUNICATIONS A. P. Wheeler, A. Veis, A. I. Caplan, Science 1992, 255, 1098 ± Structural Characterization of a Cationic 1105. [4] P. Calvert, P. -
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. -
Organometallic and Catalysis
ORGANOMETALLIC AND CATALYSIS Dr. Malay Dolai, Assistant Professor, Department of Chemistry, Prabhat Kumar College, Contai, Purba Medinipur-721404, WB, India. 1.Introduction Organometallic chemistry is the study of organometallic compounds, chemical compounds containing at least one chemical bond between a carbon atom of an organic molecule and a metal, including alkaline, alkaline earth, and transition metals, and sometimes broadened to include metalloids like boron, silicon, and tin, as well. Aside from bonds to organyl fragments or molecules, bonds to 'inorganic' carbon, like carbon monoxide (metal carbonyls), cyanide, or carbide, are generally considered to be organometallic as well. Some related compounds such as transition metal hydrides and metal phosphine complexes are often included in discussions of organometallic compounds, though strictly speaking, they are not necessarily organometallic. The related but distinct term "metalorganic compound" refers to metal-containing compounds lacking direct metal-carbon bonds but which contain organic ligands. In 1827, Zeise's salt is the first platinum- olefin complex: K[PtCl3(C2H4)].H2O, the first invented organometallic compound. Organometallic compounds find wide use in commercial reactions, both as homogeneous catalysis and as stoichiometric reagents For instance, organolithium, organomagnesium, and organoaluminium compounds, examples of which are highly basic and highly reducing, are useful stoichiometrically, but also catalyze many polymerization reactions. Almost all processes involving carbon monoxide rely on catalysts, notable examples being described as carbonylations. The production of acetic acid from methanol and carbon monoxide is catalyzed via metal carbonyl complexes in the Monsanto process and Cativa process. Most synthetic aldehydes are produced via hydroformylation. The bulk of the synthetic alcohols, at least those larger than ethanol, are produced by hydrogenation of hydroformylation- derived aldehydes. -
Nbcl5-Mg Reagent System in Regio- and Stereoselective Synthesis of (2Z)-Alkenylamines and (3Z)-Alkenylols from Substituted 2-Alkynylamines and 3-Alkynylols
molecules Article NbCl5-Mg Reagent System in Regio- and Stereoselective Synthesis of (2Z)-Alkenylamines and (3Z)-Alkenylols from Substituted 2-Alkynylamines and 3-Alkynylols Rita N. Kadikova *, Azat M. Gabdullin, Oleg S. Mozgovoj, Ilfir R. Ramazanov and Usein M. Dzhemilev Institute of Petrochemistry and Catalysis of Russian Academy of Sciences, 141 Prospekt Oktyabrya, 450075 Ufa, Russia; [email protected] (A.M.G.); [email protected] (O.S.M.); ilfi[email protected] (I.R.R.); [email protected] (U.M.D.) * Correspondence: [email protected] Abstract: The reduction of N,N-disubstituted 2-alkynylamines and substituted 3-alkynylols using the NbCl5–Mg reagent system affords the corresponding dideuterated (2Z)-alkenylamine and (3Z)- alkenylol derivatives in high yields in a regio- and stereoselective manner through the deuterolysis (or hydrolysis). The reaction of substituted propargylamines and homopropargylic alcohols with the in situ generated low-valent niobium complex (based on the reaction of NbCl5 with magnesium metal) is an efficient tool for the synthesis of allylamines and homoallylic alcohols bearing a 1,2-disubstituted double bond. It was found that the well-known approach for the reduction of alkynes based on the use of the TaCl5-Mg reagent system does not work for 2-alkynylamines and 3-alkynylols. Thus, this article reveals a difference in the behavior of two reagent systems—NbCl5-Mg and TaCl5-Mg, Citation: Kadikova, R.N.; Gabdullin, in relation to oxygen- and nitrogen-containing alkynes. A regio- and stereoselective method was A.M.; Mozgovoj, O.S.; Ramazanov, developed for the synthesis of nitrogen-containing E-β-chlorovinyl sulfides based on the reaction of I.R.; Dzhemilev, U.M. -
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. -
1-Butanol Dehydration and Dehydrogenation Over Vanadium Aluminium Oxynitride Catalysts
ACADEMIA ROMÂNĂ Rev. Roum. Chim., Revue Roumaine de Chimie 2011, 56(2), 151-159 http://web.icf.ro/rrch/ 1-BUTANOL DEHYDRATION AND DEHYDROGENATION OVER VANADIUM ALUMINIUM OXYNITRIDE CATALYSTS Mihaela FLOREA,a* Stephanie DELSARTE,b Elisabeth van KEULENb and Paul GRANGEb** aDepartment of Chemical Technology and Catalysis, Faculty of Chemistry, University of Bucharest, B-dul Regina Elisabeta 4-12, Bucharest 030018, Roumania bCatalyse et chimie des matériaux divisés, Université catholique de Louvain, Croix du Sud 2, Boite 17, Louvain-la-Neuve, 1348, Belgium Received July 5, 2010 Amorphous high surface area vanadium aluminium oxynitrides (VAlON) are prepared by nitridation of vanadium aluminium oxide precursors. The acid-base and redox properties of VAlON depend on their nitrogen content, as well as on the V/Al ratio of the reactive precursor. The influence of these parameters over the catalytic properties of VAlON for 1-butanol dehydration/dehydrogenation was studied. For the studied samples, the only detected products were 1-butene, butane and butanal. The presence of butane as a major product could be explained by a hydrogen transfer mechanism. INTRODUCTION∗ nitrogen species, may cause important differences in the catalytic behavior .6 Oxynitride systems become extensively studied The reactivity of 1-butanol over catalysts has as a new class of catalysts because of their been extensively used to evaluate the nature, the particular acid-base properties. Nitridation of strength and the concentration of the acid-base amorphous oxide precursors induces a decrease of sites 7-10 since the product selectivities are the number of acid sites and the creation of basic influenced by the acid-base properties of the centers as is shown for aluminophosphate catalysts.