Presidential Green Chemistry Challenge Awards Program: Summary of 2000 Award Entries and Recipients
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Synthesis of Protected 2′-Deoxy-2′-Fluoro-Β-D-Arabinonucleosides
Synthesis of Protected UNIT 1.7 2′-Deoxy-2′-fluoro-β-D-arabinonucleosides This unit describes in detail the preparation of protected 2′-deoxy-2′-fluoroarabinonu- cleosides. These building blocks are required for the synthesis of 2′-deoxy-2′-fluoroarabi- nonucleic acid (2′F-ANA), an oligonucleotide analog exhibiting very promising antisense properties (Damha et al., 1998; Wilds and Damha, 2000; Lok et al., 2002). The preparation of phosphoramidites from these building blocks and the synthesis of 2′F-ANA are described in UNIT 4.15. SYNTHESIS AND CHARACTERIZATION OF N2-ISOBUTYRYL-9- BASIC [2-DEOXY-2-FLUORO-5-O-(4-METHOXYTRITYL)-β-D- PROTOCOL 1 ARABINOFURANOSYL]GUANINE Synthesis of araF-G (S.6; Figure 1.7.3) was accomplished via the condensation of 2,6-dichloropurine with either 2-deoxy-2-fluoro-1,3,5-tri-O-benzoyl-α-D-arabinofura- nose (S.2; Figure 1.7.1) or 2-deoxy-2-fluoro-3,5-di-O-benzoyl-α-D-arabinofuranosyl bromide (S.3) as a key chemical step (Figure 1.7.2). Starting from S.3 gives a higher yield of S.4 and simplifies its purification. The versatile intermediate N9-β-glycoside (S.4) was transformed into araF-G in three steps (Figure 1.7.3). Treatment of S.4 with NaN3 in ethanol gave the 2,6-diazido derivative (Wower et al., 1994). This product was then subjected to reduction with SnCl2 in a mixture of dichloromethane/methanol to give its 2,6-diamino derivative (Tennila et al., 2000). Standard debenzoylation and deamination gave araF-G. -
Carbon–Fluorine Bond Formation
Carbon–Fluorine Bond Formation The Harvard community has made this article openly available. Please share how this access benefits you. Your story matters Citation Furuya, Takeru, Christian A. Kuttruff, and Tobias Ritter. 2008. Carbon–fluorine bond formation. Current Opinion in Drug Discovery and Development 11(6): 803–819. Citable link http://nrs.harvard.edu/urn-3:HUL.InstRepos:8301597 Terms of Use This article was downloaded from Harvard University’s DASH repository, and is made available under the terms and conditions applicable to Open Access Policy Articles, as set forth at http:// nrs.harvard.edu/urn-3:HUL.InstRepos:dash.current.terms-of- use#OAP Carbon–Fluorine Bond Formation Takeru Furuya, Christian A. Kuttruff, and Tobias Ritter* Department of Chemistry and Chemical Biology Harvard University 12 Oxford Street Cambridge, MA 02138 [email protected] Phone 617 496 0750 Fax 617 496 4591 1 Abstract We present a selection of carbon–fluorine bond formations that have been developed in the recent past. An overview of the most common fluorination reagents is followed by fluorination reactions organized by reactivity. We have distinguished between nucleophilic and electrophilic fluorinations as well as aliphatic and aromatic fluorinations. Each section is divided into more specific reaction classes and examples for syntheses of pharmaceuticals, 18F-radiolabeling, and mechanistic investigations are provided. Keywords Fluorination; carbon–fluorine bond formation; nucleophilic fluorination; electrophilic fluorination; fluorinating -
Gas Conversion Factor for 300 Series
300GasTable Rec # Gas Symbol GCF Density (g/L) Density (g/L) 25° C / 1 atm 0° C / 1 atm 1 Acetic Acid C2H4F2 0.4155 2.7 2.947 2 Acetic Anhydride C4H6O3 0.258 4.173 4.555 3 Acetone C3H6O 0.3556 2.374 2.591 4 Acetonitryl C2H3N 0.5178 1.678 1.832 5 Acetylene C2H2 0.6255 1.064 1.162 6 Air Air 1.0015 1.185 1.293 7 Allene C3H4 0.4514 1.638 1.787 8 Ammonia NH3 0.7807 0.696 0.76 9 Argon Ar 1.4047 1.633 1.782 10 Arsine AsH3 0.7592 3.186 3.478 11 Benzene C6H6 0.3057 3.193 3.485 12 Boron Trichloride BCl3 0.4421 4.789 5.228 13 Boron Triflouride BF3 0.5431 2.772 3.025 14 Bromine Br2 0.8007 6.532 7.13 15 Bromochlorodifluoromethane CBrClF2 0.3684 6.759 7.378 16 Bromodifluoromethane CHBrF2 0.4644 5.351 5.841 17 Bromotrifluormethane CBrF3 0.3943 6.087 6.644 18 Butane C4H10 0.2622 2.376 2.593 19 Butanol C4H10O 0.2406 3.03 3.307 20 Butene C4H8 0.3056 2.293 2.503 21 Carbon Dioxide CO2 0.7526 1.799 1.964 22 Carbon Disulfide CS2 0.616 3.112 3.397 23 Carbon Monoxide CO 1.0012 1.145 1.25 24 Carbon Tetrachloride CCl4 0.3333 6.287 6.863 25 Carbonyl Sulfide COS 0.668 2.456 2.68 26 Chlorine Cl2 0.8451 2.898 3.163 27 Chlorine Trifluoride ClF3 0.4496 3.779 4.125 28 Chlorobenzene C6H5Cl 0.2614 4.601 5.022 29 Chlorodifluoroethane C2H3ClF2 0.3216 4.108 4.484 30 Chloroform CHCl3 0.4192 4.879 5.326 31 Chloropentafluoroethane C2ClF5 0.2437 6.314 6.892 32 Chloropropane C3H7Cl 0.308 3.21 3.504 33 Cisbutene C4H8 0.3004 2.293 2.503 34 Cyanogen C2N2 0.4924 2.127 2.322 35 Cyanogen Chloride ClCN 0.6486 2.513 2.743 36 Cyclobutane C4H8 0.3562 2.293 2.503 37 Cyclopropane C3H6 0.4562 -
Oxidation Trifluoride (DAST) Selectfluor™
Vol. 5 No. 1 Synthetic Methods Iodotoluene difluoride Diethylaminosulfur Oxidation trifluoride (DAST) Selectfluor™ Ishikawa’s Reagent Other Reagents for Fluorination Dess–Martin Periodinane Bis(pyridine)iodonium tetrafluoroborate Magnesium bis(monoperoxyphthalate) hexahydrate Chloramine-T Other Reagents for Oxidation Advancing Science 2 Introduction Oxidation is one of the most common transformations in all of organic chemistry. As a result, the number of oxidizing agents and reactions at the research chemist’s disposal number in the hundreds; Sigma-Aldrich is proud to offer a new series of ChemFiles—called however, few provide extended utility across a broad range of Synthetic Methods—to our Organic Chemistry and Drug Discovery substrates while remaining able to selectively oxidize one group customers. Each piece will highlight a specific motif or selected over another. Fewer yet remain effective under mild conditions. At organic transformation, and the range of products Sigma-Aldrich Sigma-Aldrich, we are committed to being your preferred supplier offers in this area. Our first installment focuses on oxidation for reagents used in oxidation—and we’d like to highlight some chemistry. In the future, we will highlight other synthetic methods new, popular, and versatile oxidation reagents in this ChemFile. such as asymmetric synthesis and reduction. We trust you will find these pieces useful, and we welcome your comments for Listed on the following pages is a selection of oxidation reagents future installments. If you cannot find a product for your specific available from Sigma-Aldrich. For a complete listing of oxidation research in organic synthesis or drug discovery, we encourage your reagents, please visit sigma-aldrich.com/oxidation. -
Linear Alpha-Olefins (681.5030)
IHS Chemical Chemical Economics Handbook Linear alpha-Olefins (681.5030) by Elvira O. Camara Greiner with Yoshio Inoguchi Sample Report from 2010 November 2010 ihs.com/chemical November 2010 LINEAR ALPHA-OLEFINS Olefins 681.5030 B Page 2 The information provided in this publication has been obtained from a variety of sources which SRI Consulting believes to be reliable. SRI Consulting makes no warranties as to the accuracy completeness or correctness of the information in this publication. Consequently SRI Consulting will not be liable for any technical inaccuracies typographical errors or omissions contained in this publication. This publication is provided without warranties of any kind either express or implied including but not limited to implied warranties of merchantability fitness for a particular purpose or non-infringement. IN NO EVENT WILL SRI CONSULTING BE LIABLE FOR ANY INCIDENTAL CONSEQUENTIAL OR INDIRECT DAMAGES (INCLUDING BUT NOT LIMITED TO DAMAGES FOR LOSS OF PROFITS BUSINESS INTERRUPTION OR THE LIKE) ARISING OUT OF THE USE OF THIS PUBLICATION EVEN IF IT WAS NOTIFIED ABOUT THE POSSIBILITY OF SUCH DAMAGES. BECAUSE SOME STATES DO NOT ALLOW THE EXCLUSION OR LIMITATION OF LIABILITY FOR CONSEQUENTIAL OR INCIDENTAL DAMAGES THE ABOVE LIMITATION MAY NOT APPLY TO YOU. IN SUCH STATES SRI CONSULTING’S LIABILITY IS LIMITED TO THE MAXIMUM EXTENT PERMITTED BY SUCH LAW. Certain statements in this publication are projections or other forward-looking statements. Any such statements contained herein are based upon SRI Consulting’s current knowledge and assumptions about future events including without limitation anticipated levels of global demand and supply expected costs trade patterns and general economic political and marketing conditions. -
Recent Developments in Ziegler-Natta Catalysts for Olefin Polymerization and Their Processes
Indian Journal of Technology Vol. 26, February 1988, pp. 53-82 Recent Developments in Ziegler-Natta Catalysts for Olefin Polymerization and Their Processes V CHANDRASEKHAR, P R SRINIVASAN & S SIVARAM* Research Centre, Indian Petrochemicals Corporation Ltd, P.O. Petrochemicals, Baroda 391346, India The chemistry of Ziegler-Natta catalysts in olefin polymerization is reviewed. Factors determining catalyst activity are identified for the current generation of high activity - high selectivity catalysts. These include the nature of transition metal, its oxidation states and the ligands around it, the nature of alkylaluminium compounds, the physical state ofthe catalyst and its dependence on the method of preparation as well as activation of support and the role ofinternal and external donors. The effect of reaction parameters on catalyst performance as well as effect of nature of catalysts on polymer properties such as molecular weight, molecular weight distribution and stereoregularity are discussed. Current developments in soluble titanium! zirconium, vanadium and magnesium-titanium catalysts are reviewed. Different classes of industrial processes for production of polyethylene and polypropylene, namely slurry phase, gas phase and solution processes are discussed, The nature of contemporary catalysts is exemplified by selected patents from current literature, The various reactor types for polyolefins and salient reactor design aspects are discussed, The dependence of polymer properties on reactor design 11:1 well as kinetic modelling and simulation of polyolefin processes are briefly reviewed. I. Introduction made the dramatic discovery that not only propylene Polyolefins are a group of bulk commodity polymers could be polymerized to high molecular weight pol comprising of polyethylenes, polypropylene, poly ymers by Ziegler catalysts but the polymer so pro (butene-I) and various copolymers ofethylene, propy duced had a highly stereo regular structure (termed lene and higher alpha olefins. -
Chemical Names and CAS Numbers Final
Chemical Abstract Chemical Formula Chemical Name Service (CAS) Number C3H8O 1‐propanol C4H7BrO2 2‐bromobutyric acid 80‐58‐0 GeH3COOH 2‐germaacetic acid C4H10 2‐methylpropane 75‐28‐5 C3H8O 2‐propanol 67‐63‐0 C6H10O3 4‐acetylbutyric acid 448671 C4H7BrO2 4‐bromobutyric acid 2623‐87‐2 CH3CHO acetaldehyde CH3CONH2 acetamide C8H9NO2 acetaminophen 103‐90‐2 − C2H3O2 acetate ion − CH3COO acetate ion C2H4O2 acetic acid 64‐19‐7 CH3COOH acetic acid (CH3)2CO acetone CH3COCl acetyl chloride C2H2 acetylene 74‐86‐2 HCCH acetylene C9H8O4 acetylsalicylic acid 50‐78‐2 H2C(CH)CN acrylonitrile C3H7NO2 Ala C3H7NO2 alanine 56‐41‐7 NaAlSi3O3 albite AlSb aluminium antimonide 25152‐52‐7 AlAs aluminium arsenide 22831‐42‐1 AlBO2 aluminium borate 61279‐70‐7 AlBO aluminium boron oxide 12041‐48‐4 AlBr3 aluminium bromide 7727‐15‐3 AlBr3•6H2O aluminium bromide hexahydrate 2149397 AlCl4Cs aluminium caesium tetrachloride 17992‐03‐9 AlCl3 aluminium chloride (anhydrous) 7446‐70‐0 AlCl3•6H2O aluminium chloride hexahydrate 7784‐13‐6 AlClO aluminium chloride oxide 13596‐11‐7 AlB2 aluminium diboride 12041‐50‐8 AlF2 aluminium difluoride 13569‐23‐8 AlF2O aluminium difluoride oxide 38344‐66‐0 AlB12 aluminium dodecaboride 12041‐54‐2 Al2F6 aluminium fluoride 17949‐86‐9 AlF3 aluminium fluoride 7784‐18‐1 Al(CHO2)3 aluminium formate 7360‐53‐4 1 of 75 Chemical Abstract Chemical Formula Chemical Name Service (CAS) Number Al(OH)3 aluminium hydroxide 21645‐51‐2 Al2I6 aluminium iodide 18898‐35‐6 AlI3 aluminium iodide 7784‐23‐8 AlBr aluminium monobromide 22359‐97‐3 AlCl aluminium monochloride -
Surfactant Book 2007
Surfactants: Strategic Personal Care Ingredients Anthony J. O’Lenick, Jr. ISBN 978-1-932633-96-2 Copyright 2014, by Anthony J. O'Lenick, Jr. This book is out of print. The copyright has reverted back to the author. It is being made available free of charge in electronic version. Please feel free to use it, download it or cite it in other publications. Allured Publishing Corporation 362 South Schmale Road, Carol Stream, IL 60188-2787 USA Tel: 630/653-2155 Fax: 630/653-2192 e-mail: [email protected] Table of Contents Preface................................................................................................................... vii About the Author ................................................................................................. viii Acknowledgments .................................................................................................. ix Chapter 1: Raw Materials for Surfactant Preparation Background ............................................................................................................. 1 Triglycerides............................................................................................................ 4 Methyl Esters ........................................................................................................ 20 Fatty Acids ............................................................................................................ 20 Natural Acids .................................................................................................... 20 Guerbet -
United States Patent (19) 11 Patent Number: 5,807,502 Wollenweber Et Al
USOO5807502A United States Patent (19) 11 Patent Number: 5,807,502 Wollenweber et al. (45) Date of Patent: Sep. 15, 1998 54 AQUEOUS FATTY ALCOHOL DISPERSIONS 4,396,524 8/1983 Hempel et al. ......................... 252/321 4,549,002 10/1985 Hoefer et al. ... - - - - - 526/209 4,600,523 7/1986 Priorr et al. ............................ 252/321 75 Inventors: Horst-Werner Wollenweber, Duesseldorf, Rainer Hoefer, Neuss; 4,976,888 12/1990 De Clercq et al. ..................... 252/358 Heinz-Guenther Schulte, Muehlheim, 5,147,412 9/1992 Klinksiek et al. .................... 23/293 R all of Germany 5,346,973 9/1994 Feustel et al. .......................... 526/209 FOREIGN PATENT DOCUMENTS 73 Assignee: Henkel Kommanditgesellschaft Auf Aktien, Duesseldorf, Germany 1297 755 3/1992 Canada. 230 977 8/1987 European Pat. Off.. 21 Appl. No.: 765,752 399 266 11/1990 European Pat. Off.. 11 90 927 4/1965 Germany. 22 PCT Filed: Jun. 12, 1995 29 OO O30 7/1980 Germany. 30 39 393 4/1981 Germany. 86 PCT No.: PCT/EP95/02260 30 O1 387 7/1981 Germany. 36 01929 7/1987 Germany. S371 Date: Dec. 20, 1996 40 06 391 9/1991 Germany. S 102(e) Date: Dec. 20, 1996 OTHER PUBLICATIONS 87 PCT Pub. No.: WO95/35143 Database WPI, Week 8323 London: Derwent Publications Ltd., AN-83–55096K, Class A97, JP58–072000 A (Daiichi PCT Pub. Date: Dec. 28, 1995 Kogyo Seiyaku), abstract. 30 Foreign Application Priority Data Primary Examiner Richard D. Lovering Jun. 20, 1994 DE Germany .......................... 44 21 270.4 ASSistant Examiner-Daniel S. Metzmaier (51) Int. Cl. ............................................... B01D 19/04 Attorney, Agent, or Firm-Ernest G. -
Hydrogenation of Methyl Laurate to Produce Lauryl Alcohol Over Cu/Zno/Al O with Methanol As the Solvent and Hydrogen Source*
Pure Appl. Chem., Vol. 84, No. 3, pp. 779–788, 2012. http://dx.doi.org/10.1351/PAC-CON-11-06-09 © 2011 IUPAC, Publication date (Web): 5 November 2011 Hydrogenation of methyl laurate to produce lauryl alcohol over Cu/ZnO/Al2O3 with methanol as the solvent and hydrogen source* Shuguang Liang, Huizhen Liu, Jinli Liu, Weitao Wang, Tao Jiang‡, Zhaofu Zhang, and Buxing Han‡ Beijing National Laboratory for Molecular Sciences, Institute of Chemistry, Chinese Academy of Sciences, Beijing 100190, China Abstract: Hydrogenation of methyl laurate was conducted over a Cu/ZnO/Al2O3 catalyst, using methanol as the solvent and hydrogen source, to give lauryl alcohol. In this process, the solvent underwent partial decomposition in contact with the catalyst to generate hydrogen, which served as the hydrogenation agent. The effect of different factors on the reaction was examined, to optimize production of lauryl alcohol with high conversion efficiency and selec- tivity. Use of methanol as the solvent not only favored the reaction, but also suppressed a side reaction involving transesterification between methyl laurate and lauryl alcohol. Under opti- mal reaction conditions, 91.8 % conversion of methyl laurate and 88.8 % yield of lauryl alcohol could be achieved. Keywords: Cu/ZnO/Al2O3; heterogeneous catalysis; hydrogenation; lauryl alcohol; methanol; methyl laurate; supercritical fluids. INTRODUCTION Fatty alcohols derived from renewable resources, such as plant oils and animal oils, have found their numerous applications in industries, mostly used as raw materials for the synthesis of surfactants or plasticizers [1,2]. Especially, the fatty-alcohol-based surfactants have gained growing significance in the detergent market in the past few years, owing to their excellent washing properties and superior biodegradability compared to conventional detergents made from petrochemicals [3]. -
Investigations Into Alkene Hydration and Alkene Oxidation Catalysis
Louisiana State University LSU Digital Commons LSU Doctoral Dissertations Graduate School 2013 Investigations into alkene hydration and alkene oxidation catalysis William Schreiter Louisiana State University and Agricultural and Mechanical College, [email protected] Follow this and additional works at: https://digitalcommons.lsu.edu/gradschool_dissertations Part of the Chemistry Commons Recommended Citation Schreiter, William, "Investigations into alkene hydration and alkene oxidation catalysis" (2013). LSU Doctoral Dissertations. 473. https://digitalcommons.lsu.edu/gradschool_dissertations/473 This Dissertation is brought to you for free and open access by the Graduate School at LSU Digital Commons. It has been accepted for inclusion in LSU Doctoral Dissertations by an authorized graduate school editor of LSU Digital Commons. For more information, please [email protected]. INVESTIGATIONS INTO ALKENE HYDRATION AND ALKENE OXIDATION CATALYSIS A Dissertation Submitted to the Graduate Faculty of the Louisiana State University and Agricultural and Mechanical College in partial fulfillment of the requirements for the degree of Doctor of Philosophy In The Department of Chemistry by William James Schreiter B. A., Lawrence University, 2004 May 2013 TABLE OF CONTENTS ABSTRACT .......................................................................................................................................v CHAPTER 1. INTRODUCTION .....................................................................................................1 1.1 Alkene -
United States Patent Office Patented Apr
2,979,495 United States Patent Office Patented Apr. 11, 1961 1. 2 a method whereby the used solvent or catalyst suspending agent in the Ziegler process for the polymerization of 2,979,495 polymerizable hydrocarbons is recovered in a purified ETHYLENE POLYMERIZATION PROCESS IN state for recycling to the process. WHICH THE KEROSENE SUSPENDING ME. 5 Other objects and advantages of the invention will DUM ES RECOVERED become apparent from the following description and ap pended claims. James V. Cavender, Jr., Texas City, Tex., assignor to According to the invention, solvent or catalyst suspend Monsantoporation of Chemical Delaware Company, St. Louis, Mo., a cor ing agent suitable for recycle to the catalyst preparation O step in the Ziegler process is prepared by subjecting used No Drawing. Fied May 14, 1956, Ser. No. 584,874 solvent or catalyst suspending agent to washing or scrub 2 Claims. (C. 260-94.9) bing with concentrated sulfuric acid. The acid-washed solvent can then be separated from the acid, washed with alkali to remove any residual traces of acid, dried, and This invention relates to the polymerization of hydro 5 distilled, or handled in any other conventional manner carbons. More particularly, it relates to an improvement to yield a product containing essentially no contaminants the process for the production of Ziegler-type polymers, so that it performs in a manner comparable to the fresh relating specifically to a method for cleaning up the cata solvent when employed in the polymerization reaction. lyst Suspending agent employed to render it suitable for The following example is presented as illustrative of recycle purposes.