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Part I: Carbonyl-Olefin Metathesis of Norbornene
Part I: Carbonyl-Olefin Metathesis of Norbornene Part II: Cyclopropenimine-Catalyzed Asymmetric Michael Reactions Zara Maxine Seibel Submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy in the Graduate School of Arts and Sciences COLUMBIA UNIVERSITY 2016 1 © 2016 Zara Maxine Seibel All Rights Reserved 2 ABSTRACT Part I: Carbonyl-Olefin Metathesis of Norbornene Part II: Cyclopropenimine-Catalyzed Asymmetric Michael Reactions Zara Maxine Seibel This thesis details progress towards the development of an organocatalytic carbonyl- olefin metathesis of norbornene. This transformation has not previously been done catalytically and has not been done in practical manner with stepwise or stoichiometric processes. Building on the previous work of the Lambert lab on the metathesis of cyclopropene and an aldehyde using a hydrazine catalyst, this work discusses efforts to expand to the less stained norbornene. Computational and experimental studies on the catalytic cycle are discussed, including detailed experimental work on how various factors affect the difficult cycloreversion step. The second portion of this thesis details the use of chiral cyclopropenimine bases as catalysts for asymmetric Michael reactions. The Lambert lab has previously developed chiral cyclopropenimine bases for glycine imine nucleophiles. The scope of these catalysts was expanded to include glycine imine derivatives in which the nitrogen atom was replaced with a carbon atom, and to include imines derived from other amino acids. i Table of Contents List of Abbreviations…………………………………………………………………………..iv Part I: Carbonyl-Olefin Metathesis…………………………………………………………… 1 Chapter 1 – Metathesis Reactions of Double Bonds………………………………………….. 1 Introduction………………………………………………………………………………. 1 Olefin Metathesis………………………………………………………………………… 2 Wittig Reaction…………………………………………………………………………... 6 Tebbe Olefination………………………………………………………………………... 9 Carbonyl-Olefin Metathesis……………………………………………………………. -
US5523508.Pdf
|||||I|| US005523508A United States Patent (19) 11 Patent Number: 5,523,508 Krawczyk et al. 45) Date of Patent: Jun. 4, 1996 (54) PROCESS FOR LINEAR ALPHA-OLEFIN 4,689,437 8/1987 Murray ... ... 585/526 PRODUCTION: ELMINATING WAX 4,716,138 12/1987 Murray ... ... 502/117 PRECIPITATION 4,822,915 4/1989 Murray ...................................... 568/13 4,879,428 11/1989 Harandi et al. ......................... 585/533 75) Inventors: Mark A. Krawczyk, Chicago; Richard OTHER PUBLICATIONS E. Marinangeli; R. Joe Lawson, both of Arlington Heights, all of Ill. Ullman's Encyclopedia of Industrial Chemistry, 5th Ed., V. A13, pp. 245 et. ff., VCH (1989). (month unknown). 73) Assignee: UOP, Des Plaines, Ill. Primary Examiner–Shrive Beck Assistant Examiner-Timothy H. Meeks (21) Appl. No.: 366,153 Attorney, Agent, or Firm-Thomas K. McBride; Eugene I. 22 Filed: Dec. 29, 1994 Snyder (51} int. Cl. ............................................. CO7C 2/24 57 ABSTRACT 52 U.S. Cl. ... - - 585/523; 585/315; 585/316; Linear alpha-olefin formation via oligomerization of ethyl 585/329; 585/522; 585/526; 585/527 ene using transition metal catalysis leads to a Schultz-Flory 58) Field of Search ..................................... 585/315, 316, distribution of oligomers. At modest temperatures formation 585/329, 522, 523, 526, 527 of heavy oligomers which are waxy solids only partly soluble in the LAO product mix causes reactor plugging and I56) References Cited curtailing the time of continuous runs. Recycling a portion U.S. PATENT DOCUMENTS of a lighter oligomeric fraction obviates this problem and 3,641,191 2/1972 Fernald et al.................... 260/683.150 permits runs uninterrupted by solids formation. -
ECO-Ssls for Pahs
Ecological Soil Screening Levels for Polycyclic Aromatic Hydrocarbons (PAHs) Interim Final OSWER Directive 9285.7-78 U.S. Environmental Protection Agency Office of Solid Waste and Emergency Response 1200 Pennsylvania Avenue, N.W. Washington, DC 20460 June 2007 This page intentionally left blank TABLE OF CONTENTS 1.0 INTRODUCTION .......................................................1 2.0 SUMMARY OF ECO-SSLs FOR PAHs......................................1 3.0 ECO-SSL FOR TERRESTRIAL PLANTS....................................4 5.0 ECO-SSL FOR AVIAN WILDLIFE.........................................8 6.0 ECO-SSL FOR MAMMALIAN WILDLIFE..................................8 6.1 Mammalian TRV ...................................................8 6.2 Estimation of Dose and Calculation of the Eco-SSL ........................9 7.0 REFERENCES .........................................................16 7.1 General PAH References ............................................16 7.2 References Used for Derivation of Plant and Soil Invertebrate Eco-SSLs ......17 7.3 References Rejected for Use in Derivation of Plant and Soil Invertebrate Eco-SSLs ...............................................................18 7.4 References Used in Derivation of Wildlife TRVs .........................25 7.5 References Rejected for Use in Derivation of Wildlife TRV ................28 i LIST OF TABLES Table 2.1 PAH Eco-SSLs (mg/kg dry weight in soil) ..............................4 Table 3.1 Plant Toxicity Data - PAHs ..........................................5 Table 4.1 -
Radical Approaches to Alangium and Mitragyna Alkaloids
Radical Approaches to Alangium and Mitragyna Alkaloids A Thesis Submitted for a PhD University of York Department of Chemistry 2010 Matthew James Palframan Abstract The work presented in this thesis has focused on the development of novel and concise syntheses of Alangium and Mitragyna alkaloids, and especial approaches towards (±)-protoemetinol (a), which is a key precursor of a range of Alangium alkaloids such as psychotrine (b) and deoxytubulosine (c). The approaches include the use of a key radical cyclisation to form the tri-cyclic core. O O O N N N O O O H H H H H H O N NH N Protoemetinol OH HO a Psychotrine Deoxytubulosine b c Chapter 1 gives a general overview of radical chemistry and it focuses on the application of radical intermolecular and intramolecular reactions in synthesis. Consideration is given to the mediator of radical reactions from the classic organotin reagents, to more recently developed alternative hydrides. An overview of previous synthetic approaches to a range of Alangium and Mitragyna alkaloids is then explored. Chapter 2 follows on from previous work within our group, involving the use of phosphorus hydride radical addition reactions, to alkenes or dienes, followed by a subsequent Horner-Wadsworth-Emmons reaction. It was expected that the tri-cyclic core of the Alangium alkaloids could be prepared by cyclisation of a 1,7-diene, using a phosphorus hydride to afford the phosphonate or phosphonothioate, however this approach was unsuccessful and it highlighted some limitations of the methodology. Chapter 3 explores the radical and ionic chemistry of a range of silanes. -
Wide Range Linear Alpha Olefin Processes
IHS Chemical Process Economics Program Consolidated Report CR001 Wide Range Linear Alpha Olefin Processes By Marianna Asaro July 2014 ihs.com/chemical IHS Chemical Process Economics Program Consolidated Report | CR001 IHS Chemical agrees to assign professionally qualified personnel to the preparation of the Process Economics Program’s reports and will perform the work in conformance with generally accepted professional standards. No other warranties expressed or implied are made. Because the reports are of an advisory nature, neither IHS Chemical nor its employees will assume any liability for the special or consequential damages arising from the Client’s use of the results contained in the reports. The Client agrees to indemnify, defend, and hold IHS Chemical, its officers, and employees harmless from any liability to any third party resulting directly or indirectly from the Client’s use of the reports or other deliverables produced by IHS Chemical pursuant to this agreement. For detailed marketing data and information, the reader is referred to one of the IHS Chemical programs specializing in marketing research. The IHS CHEMICAL ECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced throughout the world. In addition the IHS DIRECTORY OF CHEMICAL PRODUCERS services provide detailed lists of chemical producers by company, product, and plant for the United States, Europe, East Asia, China, India, South & Central America, the Middle East & Africa, Canada, and Mexico. July 2014 ii © 2014 IHS IHS Chemical Process Economics Program Consolidated Report | CR001 PEP Report CR001 Wide Range Linear Alpha Olefin Processes By Marianna Asaro July 2014 Abstract This report consolidates and updates the Process Economics Program’s technical and economic analyses of wide-range linear alpha olefins (LAO) manufacturing technologies since PEP first reported on the subject in the 1960s. -
Self-Metathesis of 1-Octene Using Alumina-Supported Re2o7 in Supercritical CO2
Top Catal DOI 10.1007/s11244-008-9154-4 ORIGINAL PAPER Self-Metathesis of 1-Octene Using Alumina-Supported Re2O7 in Supercritical CO2 Massimo Fabris Æ Cindy Aquino Æ Antony J. Ward Æ Alvise Perosa Æ Thomas Maschmeyer Æ Maurizio Selva Ó Springer Science+Business Media, LLC 2009 Abstract In this contribution we describe the use of basic science has been applied for the benefit of man, heterogeneous catalysts for the liquid-phase self-metathesis society and the environment’’.1 Their contribution was of 1-octene in supercritical CO2. Our work aims at recognized for understanding the mechanism, and for addressing the mass-transfer problems associated with such developing very efficient and selective discrete metal- reaction systems. By coupling a heterogeneous supported based catalysts. Re2O7 catalyst with the use of scCO2, the self-metathesis Nonetheless, one should not forget that the metathesis of 1-octene takes place by and large much more rapidly reaction using heterogeneous catalysis has been an estab- than in traditional solvent media, and furthermore, by using lished industrial process since 1966, based on the use of scCO2 the overall efficiency and sustainability of the supported (usually on silica and alumina) metal oxides transformation can be improved. such as tungsten, nickel, cobalt, rhenium, and molybde- num. Three significant examples come to mind and are Keywords Metathesis Á 1-Octene Á Supercritical CO2 Á here recalled briefly. [1]. Re/Al O 2 3 1. The historic Phillips triolefin process for the produc- tion of ethene and 2-butene from propene using a WO /SiO catalyst, [2] that was shut down in 1972 1 Introduction 3 2 after 6 years of operation due to increased demand for propene, and later reutilized in the reverse direction to The metathesis of olefins is a very elegant and widely produce propene. -
Metathesis of 1-Hexene Over Heterogeneous Tungsten-Based Catalysts
METATHESIS OF 1-HEXENE OVER HETEROGENEOUS TUNGSTEN-BASED CATALYSTS Arisha Prithipal [BSc. (Eng)] In fulfilment of the requirements for the degree of Master of Science in Engineering at the School of Chemical Engineering, University of KwaZulu-Natal March, 2013 Supervisor: Prof. M. Starzak Co-Supervisor: Dr. D. Lokhat The financial assistance of the National Research Foundation (NRF) towards this research is hereby acknowledged. Opinions expressed and conclusions arrived at, are those of the author and are not necessarily to be attributed to the NRF. As the candidate’s Supervisor I agree to the submission of this thesis: ______________________________ _____________________________ Professor M. Starzak Dr. D. Lokhat DECLARATION I, Arisha Prithipal declare that (i) The research reported in this dissertation/thesis, except where otherwise indicated, is my original work. (ii) This dissertation/thesis has not been submitted for any degree or examination at any other university. (iii) This dissertation/thesis does not contain other persons’ data, pictures, graphs or other information, unless specifically acknowledged as being sourced from other persons. (iv) This dissertation/thesis does not contain other persons’ writing, unless specifically acknowledged as being sourced from other researchers. Where other written sources have been quoted, then: a) their words have been re-written but the general information attributed to them has been referenced; b) where their exact words have been used, their writing has been placed inside quotation marks, and referenced. (v) Where I have reproduced a publication of which I am an author, co-author or editor, I have indicated in detail which part of the publication was actually written by myself alone and have fully referenced such publications. -
Properties and Synthesis. Elimination Reactions of Alkyl Halides
P1: PBU/OVY P2: PBU/OVY QC: PBU/OVY T1: PBU Printer: Bind Rite JWCL234-07 JWCL234-Solomons-v1 December 8, 2009 21:37 7 ALKENES AND ALKYNES I: PROPERTIES AND SYNTHESIS. ELIMINATION REACTIONS OF ALKYL HALIDES SOLUTIONS TO PROBLEMS 7.1 (a) ( E )-1-Bromo-1-chloro-1-pentene or ( E )-1-Bromo-1-chloropent-1-ene (b) ( E )-2-Bromo-1-chloro-1-iodo-1-butene or ( E )-2-Bromo-1-chloro-1-iodobut-1-ene (c) ( Z )-3,5-Dimethyl-2-hexene or ( Z )-3,5-Dimethylhex-2-ene (d) ( Z )-1-Chloro-1-iodo-2-methyl-1-butene or ( Z )-1-Chloro-1-iodo-2-methylbut-1-ene (e) ( Z,4 S )-3,4-Dimethyl-2-hexene or ( Z,4 S )-3,4-Dimethylhex-2-ene (f) ( Z,3 S )-1-Bromo-2-chloro-3-methyl-1-hexene or (Z,3 S )-1-Bromo-2-chloro-3-methylhex-1-ene 7.2 < < Order of increasing stability 7.3 (a), (b) H − 2 ∆ H° = − 119 kJ mol 1 Pt 2-Methyl-1-butene pressure (disubstituted) H2 − ∆ H° = − 127 kJ mol 1 Pt 3-Methyl-1-butene pressure (monosubstituted) H2 − ∆ H° = − 113 kJ mol 1 Pt 2-Methyl-2-butene pressure (trisubstituted) (c) Yes, because hydrogenation converts each alkene into the same product. 106 CONFIRMING PAGES P1: PBU/OVY P2: PBU/OVY QC: PBU/OVY T1: PBU Printer: Bind Rite JWCL234-07 JWCL234-Solomons-v1 December 8, 2009 21:37 ALKENES AND ALKYNES I: PROPERTIES AND SYNTHESIS 107 H H (d) > > H H H (trisubstituted) (disubstituted) (monosubstituted) Notice that this predicted order of stability is confirmed by the heats of hydro- genation. -
United States Patent (19) 11 3,968,133 Knifton (45) July 6, 1976
United States Patent (19) 11 3,968,133 Knifton (45) July 6, 1976 54 CARBOXYLATION PROCESS FOR 3,723,486 3/1973 Kajimoto...................... 260/410.9 R PREPARING LINEAR FATTY ACDS OR 3,776,929 12/1973 Mrowca....................... 260/410.9 R ESTERS 3,819,669 6/1974 Knifton........................ 260/410.9 R 3,832,391 8/1974 Parshall........................ 260/410.9 R (75) Inventor: John F. Knifton, Poughouag, N.Y. Primary Examiner-Patrick P. Garvin 73 Assignee: Texaco Inc., New York, N.Y. Assistant Examiner-John F. Niebling 22) Filed: Nov. 25, 1974 Attorney, Agent, or Firm-T. H. Whaley; C. G. Ries; (21) Appl. No.: 526,867 Bernard Marlowe 52) U.S. C. ......................... 260/410.9 R; 260/413; 57 ABSTRACT 260/497 A; 260/488 K; 260/491; 260/.532; This invention concerns a process for preparing linear 260/533 A fatty (carboxylic) acids and esters from the reaction of 51 Int. Cl’............................................ C11C 3/02 olefins, alcohols (or water) and carbon monoxide. The (58) Field of Search......... 260/410.9 R, 413, 497 A, process is catalyzed by catalytic amounts of disper 260/488 K, 491, 532,533 A sions of ligand-stabilized, palladium(II) halide com plexes, in quaternary ammonium, phosphonium or ar 56 References Cited sonium salts of trihalostannate(II) or trihaloger UNITED STATES PATENTS manate(II). These empirically selected palladium cata 3,437,676 4/1969 Kutepow...................... 260/410.9 R lysts can be recycled with fresh olefin feed several 3,530, 155 9/1970 Fenton......................... 260/410.9 R times before substantial loss of catalytic activity is 3,530,168 9/1970 Biale..... -
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. -
Copolymerization of Ethylene and 1-Hexene with Et(Ind)
Polymer 42 2001) 6355±6361 www.elsevier.nl/locate/polymer Copolymerization of ethylene and 1-hexene with EtInd)2ZrCl2 in hexane Mauricio L. Brittoa,1, Griselda B. Gallanda, JoaÄo Henrique Z. dos Santosa,*, Madalena C. Forteb aInstituto de QuõÂmica, Universidade Federal do Rio Grande do Sul, Av. Bento GoncËalves, 9500-Porto Alegre, 91509-900 Brazil bEscola de Engenharia, Dept. de Materiais, Universidade Federal do Rio Grande do Sul, Rua Osvaldo Cruz, 99-Porto Alegre, 90035-190 Brazil Received 2 October 2000; received in revised form 5 January 2001; accepted 6 February 2001 Abstract Copolymerizations of ethylene and 1-hexene were carried out in hexane at 608C by using ethylenebisindenyl)zirconium dichloride as catalyst and methylaluminoxane MAO) as cocatalyst in presence of triisobutylaluminum TIBA). The in¯uence of the alkylaluminum concentration and AlTOTAL/Zr molar ratio on the catalyst activity and comonomer incorporation are evaluated. Increasing the TIBA concen- tration, the MAO solubility augments in the polymerization milieu, as well as the catalyst activity and the comonomer incorporation. Increasing the AlTOTAL/Zr molar ratio, catalyst activity becomes higher, while comonomer incorporation remained constant at around 8 wt% for molar ratios between 0 and 5000. For AlTOTAL/Zr molar ratios higher than 5,000 comonomer incorporation increased gradually. Under the same experimental conditions dimethylsilylbisindenyl)zirconium dichloride showed higher thermal stability and led to higher comonomer incorporation. q 2001 Published by Elsevier Science Ltd. Keywords: Metallocene; MAO; Ethylene±1-hexene copolymerization 1. Introduction discovery of the metallocene/methylaluminoxane MAO) catalyst system by Sinn and Kaminsky, a great amount of Global linear low density polyethylene LLDPE) both industrial and academic research has been done. -
Process Economics Program (PEP): Wide Range Linear Alpha Olefin Processes & On-Purpose Linear Alpha Olefin Processes PEP CR001 & CR002 Prospectus
IHS CHEMICAL Process Economics Program (PEP): Wide Range Linear Alpha Olefin Processes & On-Purpose Linear Alpha Olefin Processes PEP CR001 & CR002 Prospectus IHS CHEMICAL PROSPECTUS PEP CR001 & CR002 Contents Contents ..................................................................................................................................... 2 Introduction ................................................................................................................................ 3 Abstract ...................................................................................................................................... 5 Key Questions Addressed in the Reports .................................................................................. 6 Deliverables ............................................................................................................................... 6 Process Technologies Reviewed in CR001 & CR002 ................................................................ 6 Table of Contents ....................................................................................................................... 7 CR001 - Wide Range Linear Alpha Olefin Processes ................................................................ 7 CR002 - On-Purpose Linear Alpha Olefin Processes .............................................................. 10 Meet the Author........................................................................................................................ 15 About the IHS Chemical Process