EP1322418A2 - Catalyseurs fixes sur support pour la metathese des olefines - Google Patents

Catalyseurs fixes sur support pour la metathese des olefines

Info

Publication number
EP1322418A2
EP1322418A2 EP01976225A EP01976225A EP1322418A2 EP 1322418 A2 EP1322418 A2 EP 1322418A2 EP 01976225 A EP01976225 A EP 01976225A EP 01976225 A EP01976225 A EP 01976225A EP 1322418 A2 EP1322418 A2 EP 1322418A2
Authority
EP
European Patent Office
Prior art keywords
groups
group
carrier
sio
metathesis
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
EP01976225A
Other languages
German (de)
English (en)
Inventor
Jean-Marie Basset
Mathieu Chabanas
Christophe Coperet
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Publication of EP1322418A2 publication Critical patent/EP1322418A2/fr
Ceased legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/1616—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts
    • B01J31/1625—Coordination complexes, e.g. organometallic complexes, immobilised on an inorganic support, e.g. ship-in-a-bottle type catalysts immobilised by covalent linkages, i.e. pendant complexes with optional linking groups
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22—Organic complexes
    • B01J31/2265—Carbenes or carbynes, i.e.(image)
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C6/00—Preparation of hydrocarbons from hydrocarbons containing a different number of carbon atoms by redistribution reactions
    • C07C6/02—Metathesis reactions at an unsaturated carbon-to-carbon bond
    • C07C6/04—Metathesis reactions at an unsaturated carbon-to-carbon bond at a carbon-to-carbon double bond
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/475—Preparation of carboxylic acid esters by splitting of carbon-to-carbon bonds and redistribution, e.g. disproportionation or migration of groups between different molecules
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/50—Redistribution or isomerisation reactions of C-C, C=C or C-C triple bonds
    • B01J2231/54—Metathesis reactions, e.g. olefin metathesis
    • B01J2231/543—Metathesis reactions, e.g. olefin metathesis alkene metathesis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/70—Oxidation reactions, e.g. epoxidation, (di)hydroxylation, dehydrogenation and analogues
    • B01J2231/74—Aziridination
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • C07C2531/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • C07C2531/12—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides

Definitions

  • the present invention relates to an olefin metathesis process in which rhenium-carbene complexes are used as catalysts which have higher activities due to the targeted fixation on the surface of a suitable carrier.
  • olefin metathesis is the reaction of two olefins with one another, whereby new olefins are formed by breaking and reforming the olefinic double bond. This is shown in simplified form in the diagram below.
  • Unsaturated polymers can also be obtained by olefin metathesis, namely by ring-opening metathesis polymerization (ROMP) of cyclic olefins and by acyclic diene metathesis polymerization (ADMET) of ⁇ -, ⁇ -dienes.
  • Examples of newer applications are the selective ring opening of cyclic olefins with acyclic olefins and ring closure reactions (RCM), with which unsaturated rings of different ring sizes can be produced, preferably using ⁇ -, ⁇ -dienes.
  • a large number of transition metal compounds are suitable as catalysts for metathesis reactions, in particular those of subgroups VI to VIII of the Periodic Table of the Elements.
  • the catalysts used can be homogeneous and heterogeneous.
  • heterogeneous olefin metathesis catalysts are used in industrial applications. These are based primarily on rhenium, molybdenum and tungsten oxides, which are generally based on oxidic supports such as SiO 2 , Al 2 O 3 , SiO 2 / Al 2 O 3 , B 2 O 3 / Al 2 O 3 / SiO 2 , Nb 2 O 5 , TiO 2 are fixed.
  • these catalysts are prepared by means of aqueous impregnation techniques, the active compounds from salts, such as NH ReO, HReO, NH WO 3 or NH MoO 3 , being fixed on the support.
  • salts such as NH ReO, HReO, NH WO 3 or NH MoO 3
  • MeReO 3 as a precursor of the active catalyst species.
  • All of the catalysts described above are notable for high activity and regenerability in reactions of sterically undemanding or nonfunctionalized olefins; However, when using such functionalized olefins, such as methyl oleate, or of sterically demanding olefins with bulky substituents and / or complete substitution of the double bond, they have to be pretreated with an alkylating agent in order to increase the activity. Commonly used alkylating agents are lead tetramethyl and tin tetramethyl.
  • protic functional groups such as -OH, -CO H or -NHR 2
  • the object of the present invention is to provide a catalyst system which is suitable for olefin metathesis and which is also particularly suitable for the use of low-reactivity functionalized olefins, without prior activation having to be carried out. Furthermore, the catalysts should preferably not deactivate spontaneously on contact with reactive functional groups on the olefins used.
  • a heterogeneous catalyst which is fixed on an inorganic support and comprises at least one active rhenium compound with at least one carbene group and, if appropriate, further functional groups, characterized in that the rhenium compound has a chemical bond, preferably a covalent bond the material used as a carrier is connected.
  • the catalyst systems mentioned above have a high activity and thus enable the use of inert, sterically hindered and or functionalized olefins in the metathesis reaction.
  • the metathesis reaction can often be carried out at low temperatures, for example room temperature.
  • the bond is preferably a covalent bond.
  • a precursor connection of the active species with the carrier is implemented according to the invention.
  • the precursor compounds have one or more reactive groups which are capable of reacting with potential groups present on the support.
  • a covalent bond is formed between the support and the metal. This can be done, for example, by splitting off one or both of the groups that react with one another.
  • the rhenium complexes used according to the invention as a precursor compound and as active species are in oxidation states III to VII, preferably IV to VII, in particular V to VII.
  • the active complex must have at least one carbene unit, so that the activity in the metathesis reaction is guaranteed.
  • This carbene unit can be introduced into the active complex by various measures.
  • the carbene unit can already be present on the precursor connection.
  • a precursor unit of the carbene function can be present on the precursor compound, from which this unit is formed during the reaction with the carrier.
  • a carbine function present on the precursor compound can be converted into a carbene function by protonation by a proton, for example, on the carrier.
  • functional groups can also be present on the precursor compound, which groups can be converted into a carbene function after the precursor has been fixed on the carrier by a suitable chemical reaction with, for example, an organometallic reagent.
  • the precursor compound preferably has at least one carbene, carbine or alkyl unit.
  • precursor compounds used according to the invention have the general formula (I)
  • R 1 to R 6 are independently selected from the group consisting of hydrogen, cyclic and acyclic, linear and branched, substituted and unsubstituted Ct-C ⁇ alkyl groups, C 2 -C 4 o-alkenyl and alkynyl groups, Cs-Cp aromatics and silyl groups.
  • R 1 to R 6 are preferably selected independently of one another from linear and branched CrCio-alkyl groups, C 2 -C 10 alkenyl and alkynyl groups and C6-C 7 aromatics. These groups can carry halogens, ester groups or silyl groups as substituents.
  • R 1 to R 6 are selected from the group consisting of methyl, ethyl, propyl, i-propyl, n-butyl, i-butyl, tert-butyl, cyclohexyl, phenyl, trialkylsilyl , and vinyl groups.
  • X is selected from the group consisting of hydrogen, halogens, oxo groups, imido groups, alkoxy groups and nitride groups.
  • the indices a, b, c and d are independently integers from 0 to 4, preferably 0 to 2, the values of the individual numbers depending on the stoichiometrically required amounts.
  • the precursor compounds are reacted with the carrier, the fixed, active complex being formed by reaction between the reactive groups.
  • the active complex has at least one carbene unit.
  • the active complex preferably has a composition corresponding to the general formula (II)
  • S is the carrier
  • R 1 to R 6 , X and a, b, c and d have the meaning defined above for formula (I), the values for a to d again resulting from the required stoichiometry.
  • the substances of the formula (II) are derived from the substances of the formula (I) in that at least one of the substituents obtained in (I) has been cleaved off or converted to another substituent, which occurs during the reaction with the carrier.
  • the active complex used in the present invention is the complex of formula (III)
  • R 1 , R 2 and R 3 are independently selected from the group consisting of linear and "branched d-Cs-alkyl groups. The best results have been obtained with a complex of formula (111) in which R 1 , R 2 and R 3 is a tert-butyl group.
  • the reactive groups which are present on the support and can react with the groups on the precursor compound can in principle be selected in accordance with their desired reactivity. Protic groups will often be present on the support.
  • the oxidic carriers preferred in the context of the present invention they will preferably have hydroxyl groups which react with the precursor compound by splitting off a proton.
  • a metal-oxygen bond is formed by which the active complex is fixed.
  • the active complexes fixed via an oxygen atom are preferred according to the invention.
  • Examples of preferred oxidic supports according to the invention include SiO 2 , Al 2 O 3 , SiO 2 / Al 2 O 3 , B 2 O 3 / Al 2 O 3 , B 2 O 3 / Al 2 O 3 / SiO 2 , NbO 2 , TiO 2 , ZrO 2 as well as zeolites and clays of natural and synthetic origin.
  • the carriers can be modified by, for example, Lewis or Bronsted acids, such as sulfate ions, BF 3 or boroganyls.
  • SiO 2 is preferably used, which can be porous or non-porous, for example mesoporous with pores of 20 to 200 ⁇ .
  • the supports can also have been treated in another suitable manner, for example by a heat treatment to remove water.
  • a heat treatment to remove water.
  • this may have been treated at temperatures of 200 to 800 ° C.
  • the heat treatments can be carried out under an inert gas atmosphere or under an oxygen atmosphere.
  • the catalysts of the formula (II) used according to the invention are prepared by reacting the precursor compound of the formula (I) with the support which has at least one suitable reactive group, as a result of which the fixed active complex is formed.
  • the reaction can be carried out in a suitable inert solvent in which the precursor compound is dispersed or dissolved and then reacted with the carrier.
  • suitable solvents or dispersants are paraffins, for example pentane, hexane or cyclohexane, ether.
  • the reaction can also be carried out by evaporating the carrier with a precursor compound which is brought into the gas phase, for example by sublimation.
  • the active complex is prepared in which a compound which contains reactive groups corresponds to the reactive Groups can react on the carrier, is implemented with this. Apart from the reactive group, this compound contains no organic functions. In general, the compounds of this type do not have any organic substituents such as carbine, carbene or alkyl functions, but possibly alkoxy, oxo, amido, imido, nitride and / or halogen atoms, if appropriate also alkyl groups.
  • the compound After being fixed on the support, the compound is then converted into the active complex, for example by alkylating reagents such as organoaluminum, organozinc and Grignard compounds, alkylidene precursor compounds such as phosphoranes and diazoalkanes, reactive and / or unsaturated hydrocarbons such as cyclopropane, cyclopropene, Alkynes, dienes, alkenes.
  • alkylating reagents such as organoaluminum, organozinc and Grignard compounds, alkylidene precursor compounds such as phosphoranes and diazoalkanes, reactive and / or unsaturated hydrocarbons such as cyclopropane, cyclopropene, Alkynes, dienes, alkenes.
  • the catalysts of the invention are extremely reactive. In principle, they can be used for all olefins, whether they are reactive or inert or, if appropriate, have further functional groups.
  • olefins can carry terminal or internal double bonds and can be cyclic or acyclic, linear or branched.
  • the total carbon number can be from 1 to 100, preferably 1 to 40; the double bonds can be unsubstituted or mono-, bi-, tri- or tetrasubstituted.
  • the olefins which can be used can also be cyclic olefins, for example cycloalkenes or cycloalkadienes. There may be further functional groups, for example further double or triple bonds. Examples of further possible substituents are aromatic functions, ester, aldehyde, keto, nitrile, amide, alcohol and amine functions, sulfur and phosphorus units.
  • the catalysts used according to the invention are furthermore suitable for use in principle in all metathesis reactions, that is to say in self-metathesis as well as in the co-metathesis of acyclic olefins, and of course also in ethenolysis. Furthermore, they can be used in the metathesis reactions explained above, which are known under the abbreviations ROMP, ADMET and RCM.
  • the olefin / catalyst ratio is from 1 to 10,000,000, preferably 2 to 100,000, particularly preferably 4 to 1,000.
  • the reaction temperature is set to values from -50 to 400 ° C., preferably 0 to 150 ° C., in particular 15 to 100 ° C.
  • the reaction can be carried out in the absence of or with a solvent.
  • a solvent is preferably aprotic and apolar. Examples include paraffins, preferably hexane and pentane, halogenated compounds, preferably dichloromethane and dichlorobenzene, and aromatic compounds, preferably toluene.
  • the solvent may have been degassed before the reaction.
  • the concentration of olefins is from 0.001 mol / 1 to 10 mol / 1, preferably 0.01 to 5 mol / 1, in particular 0.1 to 2 mol / 1.
  • the reaction can be carried out continuously or batchwise.
  • Example 6 Conversion of pent-2-nitrile

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

L'invention concerne un nouveau catalyseur hétérogène, adapté en particulier à la métathèse des oléfines. Ce catalyseur est fixé sur un support inorganique et il contient au moins un composé actif de rhénium comportant au moins un groupe carbène, ainsi qu'éventuellement d'autres groupes fonctionnels. Le composé de rhénium est lié par liaison chimique au matériau utilisé comme support.
EP01976225A 2000-09-15 2001-09-14 Catalyseurs fixes sur support pour la metathese des olefines Ceased EP1322418A2 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10046143A DE10046143A1 (de) 2000-09-15 2000-09-15 Trägerfixierte Katalysatoren für die Olefin-Metathese
DE10046143 2000-09-15
PCT/EP2001/010675 WO2002022262A2 (fr) 2000-09-15 2001-09-14 Catalyseurs fixes sur support pour la metathese des olefines

Publications (1)

Publication Number Publication Date
EP1322418A2 true EP1322418A2 (fr) 2003-07-02

Family

ID=7656654

Family Applications (1)

Application Number Title Priority Date Filing Date
EP01976225A Ceased EP1322418A2 (fr) 2000-09-15 2001-09-14 Catalyseurs fixes sur support pour la metathese des olefines

Country Status (9)

Country Link
US (1) US6878660B2 (fr)
EP (1) EP1322418A2 (fr)
JP (1) JP2004508191A (fr)
CN (1) CN1457272A (fr)
AU (1) AU2001295565A1 (fr)
CA (1) CA2422594A1 (fr)
DE (1) DE10046143A1 (fr)
WO (1) WO2002022262A2 (fr)
ZA (1) ZA200302067B (fr)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120289617A1 (en) * 2011-05-10 2012-11-15 Saudi Arabian Oil Company Hybrid Catalyst for Olefin Metathesis
DE102014105885A1 (de) * 2014-04-25 2015-10-29 Universität Stuttgart N-Heterozyklische Carbenkomplexe von Metallimidoalkylidenen und Metalloxoalkylidenen und deren Verwendung
CN104311378B (zh) * 2014-11-11 2016-02-24 万华化学集团股份有限公司 一种制备新己烯及其催化剂的制备方法
US10308572B2 (en) 2015-06-25 2019-06-04 King Abdullah University Of Science And Technology Process for compound transformation

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5905055A (en) * 1994-05-03 1999-05-18 Dsm N.V. Heterogeneous metathesis catalyst

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2525224A1 (fr) 1982-04-14 1983-10-21 Rhone Poulenc Chim Base Nouveaux complexes de metaux de transition coordones avec un acide de lewis, procede de preparation de ces complexes, utilisation de ces complexes en tant que catalyseurs dans la reaction de metathese des olefines
US4818442A (en) 1984-10-09 1989-04-04 Phillips Petroleum Company Disproportionation process
US5342985A (en) * 1988-12-10 1994-08-30 Hoechst Ag Organic derivatives of rhenium oxides and their preparation and use for the metathesis of olefins
US5087710A (en) 1990-01-04 1992-02-11 Massachusetts Institute Of Technology Homogeneous rhenium catalysts for metathesis of olefins
US5146033A (en) * 1990-01-04 1992-09-08 Massachusetts Institute Of Technology Homogeneous rhenium catalysts for metathesis of olefins
FI84562C (fi) * 1990-01-16 1991-12-27 Neste Oy Foerfarande och anordning foer framstaellning av heterogena katalysatorer.
US5175311A (en) * 1990-03-29 1992-12-29 Research Corporation Technologies, Inc. Method of enantioselective cyclopropanation using chiral catalysts
US5198511A (en) * 1991-12-20 1993-03-30 Minnesota Mining And Manufacturing Company Polymerizable compositions containing olefin metathesis catalysts and cocatalysts, and methods of use therefor
JP3521912B2 (ja) * 1993-12-30 2004-04-26 エクソンモービル・ケミカル・パテンツ・インク トランス非共役ジオレフィンの合成方法
FR2750894B1 (fr) 1996-07-12 1998-11-06 Centre Nat Rech Scient Procede de metathese d'alcanes et son catalyseur
DE19932060A1 (de) * 1999-07-12 2001-01-18 Basf Ag Verfahren zur Herstellung von C¶5¶-/C¶6¶-Olefinen

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5905055A (en) * 1994-05-03 1999-05-18 Dsm N.V. Heterogeneous metathesis catalyst

Non-Patent Citations (14)

* Cited by examiner, † Cited by third party
Title
B. CORNILS, W.A. HERRRMANN (EDS.): "Applied Homogeneous Catalysis with Organometallic Compounds", 2002, WILEY-VCH VERLAG GMBH, WEINHEIM (DE) *
BRÉGEAULT J-M ET AL: "Novel Rhenium Catalysts (Chlorides and/or Alkoxides Dispersed on Inorganic Supports) for Metathesis: A Comparison with Ammonium Perrhenate Precursors", J. MOL. CATAL., vol. 46, 1988, pages 37 - 60 *
BUFFON R ET AL: "A SURFACE ORGANOMETALLIC APPROACH TO THE SYNTHESIS OF RHENIUM-BASED CATALYSTS FOR THE METATHESIS OF OLEFINS: CH3REO3/NB2O5", JOURNAL OF MOLECULAR CATALYSIS, vol. 76, 1992, pages 287 - 295, XP009005522 *
BUFFON R ET AL: "Surface organometallic chemistry of rhenium: attempts to characterize a surface carbene in metathesis of olefins with the catalyst CH3ReO3/Nb2O5", J. MOL. CATAL., vol. 72, 1992, pages L7 - L10 *
ESPEUSON J H ET AL: "Proton-Deuteron Exchange Reactions of Methyltrioxorhenium(VII) in Organic Solvents", ORGANOMETALLICS, vol. 24, 22 April 2005 (2005-04-22), pages 2780 - 2788 *
FLATT B T ET AL: "Synthesis, Structure, and Reactivity of a Rhenium Oxo-Vinylalkylidene Complex", ORGANOMETALLICS, vol. 13, no. 7, 1994, pages 2728 - 2732 *
GREENLEE W S ET AL: "Olefin Metathesis by Rhenium Carbonyl Halide-Alkylaluminum Halide Catalysts. Direct Evidence for a Coordinated Carbene Initiated Process", INORG. CHEM., vol. 15, no. 9, 1976, pages 2129 - 2134 *
KIRLIN P S ET AL: "A Stable Supported Re Metathesis Catalyst derived from [Re(CO)3OH]4 on SiO2", J. CHEM. SOC., CHEM. COMMUN., 1985, pages 277 - 279 *
KÜHN F E ET AL: "Methyltrioxorhenium and its applications in olefin oxidation, metathesis and aldehyde olefination", J. ORGANOMET. CHEM., vol. 689, 17 September 2004 (2004-09-17), pages 4149 - 4164, XP004650661, DOI: doi:10.1016/j.jorganchem.2004.08.018 *
MORRIS L J ET AL: "Photo-induced tautomerisation of methyltrioxorhenium(VII): the intermediate in olefin-metathesis?", CHEMICAL COMMUNICATIONS, no. 1, 7 January 2000 (2000-01-07), pages 67 - 68 *
NICOLAIDES C P ET AL: "An Alumina-supported Alkene Metathesis Catalyst Prepared from [Re(CO)5Br]", J. MOL. CATAL., vol. 35, 1986, pages 391 - 395 *
REED C A: "Carboranes: A New Class of Weakly Coordinating Anions for Strong Electrophiles, Oxidants, and Superacids", ACC. CHEM. RES., vol. 31, 1998, pages 133 - 139, XP000982013, DOI: doi:10.1021/ar970230r *
SCHAVERIEN, COLIN J. ET AL: "A Well-Characterized, Highly Active, Lewis Acid Free Olefin Metathesis Catalyst", JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, vol. 108, no. 10, 1986, pages 2771 - 2773, XP002643012 *
WARWEL S: "Industrielle Prozesse der Olefin-Metathese", PETROCHEMIE, vol. 103, no. 5, 1987, pages 238 - 245 *

Also Published As

Publication number Publication date
DE10046143A1 (de) 2002-05-29
JP2004508191A (ja) 2004-03-18
ZA200302067B (en) 2004-04-01
AU2001295565A1 (en) 2002-03-26
US20030181776A1 (en) 2003-09-25
US6878660B2 (en) 2005-04-12
CN1457272A (zh) 2003-11-19
WO2002022262A2 (fr) 2002-03-21
WO2002022262A3 (fr) 2002-10-24
CA2422594A1 (fr) 2003-03-14

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