Homogeneous Chromium Catalysts for Olefin Polymerization
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Opportunities for Catalysis in the 21St Century
Opportunities for Catalysis in The 21st Century A Report from the Basic Energy Sciences Advisory Committee BASIC ENERGY SCIENCES ADVISORY COMMITTEE SUBPANEL WORKSHOP REPORT Opportunities for Catalysis in the 21st Century May 14-16, 2002 Workshop Chair Professor J. M. White University of Texas Writing Group Chair Professor John Bercaw California Institute of Technology This page is intentionally left blank. Contents Executive Summary........................................................................................... v A Grand Challenge....................................................................................................... v The Present Opportunity .............................................................................................. v The Importance of Catalysis Science to DOE.............................................................. vi A Recommendation for Increased Federal Investment in Catalysis Research............. vi I. Introduction................................................................................................ 1 A. Background, Structure, and Organization of the Workshop .................................. 1 B. Recent Advances in Experimental and Theoretical Methods ................................ 1 C. The Grand Challenge ............................................................................................. 2 D. Enabling Approaches for Progress in Catalysis ..................................................... 3 E. Consensus Observations and Recommendations.................................................. -
© Copyright 2013 Jennifer L. Steele
© Copyright 2013 Jennifer L. Steele DIVALENT TRANSITION METAL CENTERS: THE SYNTHESIS OF NEW CHEMICAL VAPOR DEPOSITION PRECURSORS AND STUDIES OF ETHYLENE POLYMERIZATION AND OLIGOMERIZATION CATALYSTS BY JENNIFER L. STEELE DISSERTATION Submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy in Chemistry in the Graduate College of the University of Illinois at Urbana-Champaign, 2013 Urbana, Illinois Doctoral Committee: Professor Gregory S. Girolami, Chair Assistant Professor Alison R. Fout Professor John A. Katzenellenbogen Professor Thomas B. Rauchfuss Abstract Volatile transition metal complexes that contain boron hydride ligands are desirable for their potential as precursors for metal diboride films for microelectronics applications. Recently our group has discovered a new class of potential precursors in the metal complexes of the chelating borohydride, N,N-dimethylaminodiboranate (DMADB). To date, attempts to synthesize homoleptic complexes of the late transition metals have afforded intractable mixtures, likely the result of overreduction of the metal center. This work has focused on the synthesis and characterization of heteroleptic complexes of the late transition metals that contain both DMADB and 1,2,3,4,5,-pentamethylcyclopentadienyl ligands. The reaction of metal complexes of the form [Cp*MX]n, where Cp* is 1,2,3,4,5,- pentamethylcyclopentadienyl, M = Cr, Fe, Co, or Ru, and X = Cl or I with sodium dimethylaminodiboranate (NaDMADB) in diethyl ether affords the divalent complexes [Cp*M(DMADB)]. Additionally, the analogous vanadium compound [Cp*V(DMADB)] can be synthesized from the reduction of [Cp*VCl2]3 with NaDMADB in diethyl ether. All of these compounds are volatile under static vacuum at room temperature, but are also thermally sensitive; the iron and ruthenium derivatives decompose at room temperature over a day. -
Chapter 2 Polymerisation of MMA Using Novel Chromium(II)
A Thesis Submitted for the Degree of PhD at the University of Warwick Permanent WRAP URL: http://wrap.warwick.ac.uk/133954 Copyright and reuse: This thesis is made available online and is protected by original copyright. Please scroll down to view the document itself. Please refer to the repository record for this item for information to help you to cite it. Our policy information is available from the repository home page. For more information, please contact the WRAP Team at: [email protected] warwick.ac.uk/lib-publications Novel chromium compounds and their use in the polymerisation of methyl methacrylate Mark Andrew Stump A Thesis submitted for the Degree of Doctor of Philosophy Department of Chemistry University of Warwick Coventry CV4 7AL 18th January 1998 A: Table of Contents A Table of Contents 1• B Table of Tables Vlll• • • C Table of Figures xiv D Declaration xix E Acknowledgements XX F Summary xxi G Abbreviations xxii 1. Introduction 2 1.1. An Introduction to Polymers 12 3 1.2. Types of Polymerisation 5 1.2.1. Anionic Polymerisation 5 1.2.2. Co-ordination Polymerisation 7 1.2.3. Radical Polymerisation 9 1.3. Controlled Polymerisation 10 1.3.1. Stereochemistry of vinyl polymerisation 10 1.3.2. Other Aspects of Controlled Polymerisation 12 1.4. Living Polymerisation 13 1.5. An Introduction To Chromium Chemistry 22 1.6. Methods of Analysis for Polymers 34 1.6.1. Size Exclusion Chromatography (SEC) 34 1.6.2. Thermal Gravimetric Analysis (TGA) 35 1.7. References 44 2. Polymerisation of MMA using novel chromium(II) and (III) compounds in conjunction with alkyl halides 49 2.1. -
Bond Distances and Bond Orders in Binuclear Metal Complexes of the First Row Transition Metals Titanium Through Zinc
Metal-Metal (MM) Bond Distances and Bond Orders in Binuclear Metal Complexes of the First Row Transition Metals Titanium Through Zinc Richard H. Duncan Lyngdoh*,a, Henry F. Schaefer III*,b and R. Bruce King*,b a Department of Chemistry, North-Eastern Hill University, Shillong 793022, India B Centre for Computational Quantum Chemistry, University of Georgia, Athens GA 30602 ABSTRACT: This survey of metal-metal (MM) bond distances in binuclear complexes of the first row 3d-block elements reviews experimental and computational research on a wide range of such systems. The metals surveyed are titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, and zinc, representing the only comprehensive presentation of such results to date. Factors impacting MM bond lengths that are discussed here include (a) n+ the formal MM bond order, (b) size of the metal ion present in the bimetallic core (M2) , (c) the metal oxidation state, (d) effects of ligand basicity, coordination mode and number, and (e) steric effects of bulky ligands. Correlations between experimental and computational findings are examined wherever possible, often yielding good agreement for MM bond lengths. The formal bond order provides a key basis for assessing experimental and computationally derived MM bond lengths. The effects of change in the metal upon MM bond length ranges in binuclear complexes suggest trends for single, double, triple, and quadruple MM bonds which are related to the available information on metal atomic radii. It emerges that while specific factors for a limited range of complexes are found to have their expected impact in many cases, the assessment of the net effect of these factors is challenging. -
1 the Structure and Reactivity of Single and Multiple
1 1 The Structure and Reactivity of Single and Multiple Sites on Heterogeneous and Homogeneous Catalysts: Analogies, Differences, and Challenges for Characterization Methods Adriano Zecchina , Silvia Bordiga , and Elena Groppo 1.1 Introduction The content of this book is specifi cally devoted to a description of the complexity of the catalytic centers (both homogeneous and heterogeneous) viewed as nanoma- chines for molecular assembling. Although the word “ nano ” is nowadays some- what abused, its use for catalysts science (as nanoscience) is fully justifi ed. It is a matter of fact that (i) to perform any specifi c catalytic action, the selective catalyst must necessarily possess sophisticated structure where substrates bonds are broken and formed along a specifi c path and (ii) the relevant part of this structure, usually constituted by a metal center or metal cluster surrounded by a sphere of ligands or by a solid framework or by a portion of functionalized surface, often reaches the nanometric dimension. As it will emerge from the various chapters, this vision is valid for many types of selective catalysts including catalysts for hydrogenation, polymerization, olygomerization, partial oxidation, and photocata- lytic solar energy conversion. Five chapters are devoted to the above - mentioned reactions. From the point of view of the general defi nition, homogeneous and heterogeneous selective catalysts can be treated in the same way. As homogeneous selective catalysts are concerned, the tridimensional structure surrounding the metal center can be organized with cavitand shape, while for heterogeneous cata- lysts the selectivity is the result of an accurate design and synthesis of the frame- work structures (often microporous and crystalline) where the sites are anchored. -
Heterogeneous Catalytic Oligomerization of Ethylene
Heterogeneous Catalytic Oligomerization of Ethylene Oliver Dennis Jan A dissertation submitted in partial fulfillment of the requirements for the degree of Doctor of Philosophy University of Washington 2017 Reading Committee: Fernando Resende, Chair Rick Gustafson Anthony Dichiara Program Authorized to Offer Degree: School of Environmental and Forest Sciences © Copyright 2017 Oliver Dennis Jan ii University of Washington Abstract Heterogeneous Catalytic Oligomerization of Ethylene Oliver Dennis Jan Chair of the Supervisory Committee: Assistant Professor Fernando Resende School of Environmental and Forest Sciences Throughout this work, we report results for the oligomerization of ethylene over Ni-Hβ in a packed bed reactor. We performed a parameterized study over temperature (30ºC-190ºC), pressure (8.5-25.6 bar), and weighted hourly space velocity (2.0-5.5 hr-1). We observed that the ethylene conversion increased with reaction pressure due primarily to the slower velocities at higher pressures. Increasing the temperature of the reactor led to the formation of larger oligomers and coke, but its effect on the conversion was small. The space velocity played an important role on ethylene conversion and product selectivity, with higher conversions observed at lower space velocities and higher selectivities to butene at higher space velocities. We also conducted a long experiment to determine the activity of the Ni-Hβ catalyst over 72 hours-on-stream at 19.0 bar partial pressure of ethylene, 120ºC, and 3.1 hr-1 WHSV. We observed that catalyst deactivation occurred only during the startup period largely due to coke formation. Despite this initial iii deactivation, negligible coke formation occurred after 8 hours time-on-stream, as the conversion remained steady at 47% for the duration of the experiment. -
Basic Research Needs for Catalysis Science
Basic Research Needs for Catalysis Science Report of the Basic Energy Sciences Workshop on Basic Research Needs for Catalysis Science to Transform Energy Technologies May 8–10, 2017 Image courtesy of Argonne National Laboratory. DISCLAIMER This report was prepared as an account of a workshop sponsored by the U.S. Department of Energy. Neither the United States Government nor any agency thereof, nor any of their employees or officers, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof. The views and opinions of document authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof. Copyrights to portions of this report (including graphics) are reserved by original copyright holders or their assignees, and are used by the Government’s license and by permission. Requests to use any images must be made to the provider identified in the image credits. This report is available in pdf format at https://science.energy.gov/bes/community-resources/reports/ REPORT OF THE BASIC RESEARCH NEEDS WORKSHOP FOR CATALYSIS SCIENCE Basic Research Needs for Catalysis Science TO TRANSFORM ENERGY TECHNOLOGIES Report from the U.S. Department of Energy, Office of Basic Energy Sciences Workshop May 8–10, 2017, in Gaithersburg, Maryland CHAIR: ASSOCIATE CHAIRS: Carl A. -
Low Cost/Waste Catalyst for Fatty Acid Methyl Ester Production
Article Number: 2AEBF76 A Paper presented at the 39th CSN Annual International Conference, Workshop and Exhibition, Rivers State University of Science and Technology, Port Harcourt, Nigeria. 18th – 23rd September 2016 Copyright ©2018 Author(s) retain the copyright of this article Conference Proceedings http://www.proceedings.academicjournals.org/ Full Length Research Paper Low cost/waste catalyst for fatty acid methyl ester production M. O. Ekeoma1*, P. A. C. Okoye2 and V. I. E. Ajiwe2 1Department of Chemistry, College of Physical and Applied Sciences, Michael Okpara University of Agriculture, Umudike, P. M. B. 7267, Umuahia, Abia State, Nigeria. 2Department of Pure and Industrial Chemistry, Faculty of Physical Sciences, Nnamdi Azikiwe University, Awka, Anambra State, Nigeria. Non-edible crude karanj (Pongamia pinnata) oil (CKO) with high free fatty acid (FFA) content was used as effective renewable feedstock for fatty acid methyl ester (FAME) production. Calcium feldspar clay, a rare compositional variety of plagioclase clay, a low cost, abundant earth resource, containing over 90% CaO and belonging to the class of anorthite clay was used as heterogeneous catalyst in direct conversion of high FFA crude karanj oil to fatty acid methyl esters. The efficiency of the catalyst was made possible by the structural rearrangement of the mixed metal oxides' content of the catalyst at prolonged high temperatures, a behaviour characteristic of glass transitions and properties of amorphous phases of plagioclase feldspar, and thus was transformed into solid acid particles such as acidic mesoporous aluminium silicate mixed oxides. Optimum FAME yield of 98.97% was obtained at 4 h reaction time, 6 wt% catalyst loading, 9:1 methanol to CKO molar ratio and at methanol reflux temperature. -
Rpt POL-TOXIC AIR POLLUTANTS 98 BY
SWCAA TOXIC AIR POLLUTANTS '98 by CAS ASIL TAP SQER CAS No HAP POLLUTANT NAME HAP CAT 24hr ug/m3 Ann ug/m3 Class lbs/yr lbs/hr none17 BN 1750 0.20 ALUMINUM compounds none0.00023 AY None None ARSENIC compounds (E649418) ARSENIC COMPOUNDS none0.12 AY 20 None BENZENE, TOLUENE, ETHYLBENZENE, XYLENES BENZENE none0.12 AY 20 None BTEX BENZENE none0.000083 AY None None CHROMIUM (VI) compounds CHROMIUM COMPOUN none0.000083 AY None None CHROMIUM compounds (E649962) CHROMIUM COMPOUN none0.0016 AY 0.5 None COKE OVEN COMPOUNDS (E649830) - CAA 112B COKE OVEN EMISSIONS none3.3 BN 175 0.02 COPPER compounds none0.67 BN 175 0.02 COTTON DUST (raw) none17 BY 1,750 0.20 CYANIDE compounds CYANIDE COMPOUNDS none33 BN 5,250 0.60 FIBROUS GLASS DUST none33 BY 5,250 0.60 FINE MINERAL FIBERS FINE MINERAL FIBERS none8.3 BN 175 0.20 FLUORIDES, as F, containing fluoride, NOS none0.00000003 AY None None FURANS, NITRO- DIOXINS/FURANS none5900 BY 43,748 5.0 HEXANE, other isomers none3.3 BN 175 0.02 IRON SALTS, soluble as Fe none00 AN None None ISOPROPYL OILS none0.5 AY None None LEAD compounds (E650002) LEAD COMPOUNDS none0.4 BY 175 0.02 MANGANESE compounds (E650010) MANGANESE COMPOU none0.33 BY 175 0.02 MERCURY compounds (E650028) MERCURY COMPOUND none33 BY 5,250 0.60 MINERAL FIBERS ((fine), incl glass, glass wool, rock wool, slag w FINE MINERAL FIBERS none0.0021 AY 0.5 None NICKEL 59 (NY059280) NICKEL COMPOUNDS none0.0021 AY 0.5 None NICKEL compounds (E650036) NICKEL COMPOUNDS none0.00000003 AY None None NITROFURANS (nitrofurans furazolidone) DIOXINS/FURANS none0.0013 -
Wavelength Dependence of Photooxidation Vs Photofragmentation of Chromocene
J. Phys. Chem. A 2001, 105, 8665-8671 8665 Wavelength Dependence of Photooxidation vs Photofragmentation of Chromocene Peter T. Muraoka, Daniel Byun, and Jeffrey I. Zink* Department of Chemistry and Biochemistry, UniVersity of California, Los Angeles, California 90095 ReceiVed: March 19, 2001; In Final Form: July 2, 2001 Photooxidation and metal-ligand photolysis reactions of bis(cyclopentadienyl)chromium, chromocene, in the range 24 390-15 630 cm-1 are studied in the gas phase by using time-of-flight mass spectroscopic detection. Photooxidation of the intact chromocene molecule unexpectedly dominates in the range 23 530-24 000 cm-1. The relative importance of photooxidation compared to photofragmentation is strongly wavelength dependent. A prominent species at all wavelengths is the chromium ion, but in a wavelength region corresponding to the lowest energy ligand to metal charge transfer excited electronic state absorption, the strongest peak is from the chromocene ion. The excitation spectra are reported for three selected species: chromocene ion, mono- (cyclopentadienyl)chromium ion, and the chromium ion. The spectrum obtained by monitoring the metal ion contains sharp peaks that are assigned to neutral chromium atom resonances. Sharp losses of intensities in the molecular ion spectra are observed at these wavelengths. The wavelength dependencies of the photoreactions are interpreted and explained in terms of the identity of the initially populated excited electronic state and the ionization energy of the molecule. When the initially populated excited electronic state is the ligand to metal charge transfer state, the first photon causes minimal bond weakening and the second photon excites the intact chromocene above the ionization energy, resulting in efficient ionization of the parent molecule. -
Rh(I) Complexes in Catalysis: a Five-Year Trend
molecules Review Rh(I) Complexes in Catalysis: A Five-Year Trend Serenella Medici * , Massimiliano Peana * , Alessio Pelucelli and Maria Antonietta Zoroddu Department of Chemistry and Pharmacy, University of Sassari, Vienna 2, 07100 Sassari, Italy; [email protected] (A.P.); [email protected] (M.A.Z.) * Correspondence: [email protected] (S.M.); [email protected] (M.P.) Abstract: Rhodium is one of the most used metals in catalysis both in laboratory reactions and industrial processes. Despite the extensive exploration on “classical” ligands carried out during the past decades in the field of rhodium-catalyzed reactions, such as phosphines, and other com- mon types of ligands including N-heterocyclic carbenes, ferrocenes, cyclopentadienyl anion and pentamethylcyclopentadienyl derivatives, etc., there is still lively research activity on this topic, with considerable efforts being made toward the synthesis of new preformed rhodium catalysts that can be both efficient and selective. Although the “golden age” of homogeneous catalysis might seem over, there is still plenty of room for improvement, especially from the point of view of a more sustainable chemistry. In this review, temporally restricted to the analysis of literature during the past five years (2015–2020), the latest findings and trends in the synthesis and applications of Rh(I) complexes to catalysis will be presented. From the analysis of the most recent literature, it seems clear that rhodium-catalyzed processes still represent a stimulating challenge for the metalloorganic chemist that is far from being over. Keywords: rhodium; catalysis; Rh(I) complexes Citation: Medici, S.; Peana, M.; Pelucelli, A.; Zoroddu, M.A. Rh(I) Complexes in Catalysis: A Five-Year 1. -
Microwave-Assisted Homogeneous Acid Catalysis and Chemoenzymatic Synthesis of Dialkyl Succinate in a Flow Reactor
catalysts Article Microwave-Assisted Homogeneous Acid Catalysis and Chemoenzymatic Synthesis of Dialkyl Succinate in a Flow Reactor Laura Daviot 1, Thomas Len 1, Carol Sze Ki Lin 2 and Christophe Len 1,3,* 1 Centre de Recherche de Royallieu, Université de Technologie Compiègne, Sorbonne Universités, Cedex BP20529, F-60205 Compiègne, France; [email protected] (L.D.); [email protected] (T.L.) 2 School of Energy and Environment, City University of Hong Kong, Tat Chee Avenue, Kowloon Tong, Hong Kong, China; [email protected] 3 Institut de Recherche de Chimie Paris, PSL Research University, Chimie ParisTech, CNRS, UMR 8247, Cedex 05, F-75231 Paris, France * Correspondence: [email protected]; Tel.: +33-144-276-752 Received: 12 February 2019; Accepted: 8 March 2019; Published: 16 March 2019 Abstract: Two new continuous flow systems for the production of dialkyl succinates were developed via the esterification of succinic acid, and via the trans-esterification of dimethyl succinate. The first microwave-assisted continuous esterification of succinic acid with H2SO4 as a chemical homogeneous catalyst was successfully achieved via a single pass (ca 320 s) at 65–115 ◦C using a MiniFlow 200ss Sairem Technology. The first continuous trans-esterification of dimethyl succinate with lipase Cal B as an enzymatic catalyst was developed using a Syrris Asia Technology, with an optimal reaction condition of 14 min at 40 ◦C. Dialkyl succinates were produced with the two technologies, but higher productivity was observed for the microwave-assisted continuous esterification using chemical catalysts. The continuous flow trans-esterification demonstrated a number of advantages, but it resulted in lower yield of the target esters.