WO2000006298A1 - Metal complexes suitable for attachment to a support and supported metal complexes - Google Patents
Metal complexes suitable for attachment to a support and supported metal complexes Download PDFInfo
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- WO2000006298A1 WO2000006298A1 PCT/GB1999/002427 GB9902427W WO0006298A1 WO 2000006298 A1 WO2000006298 A1 WO 2000006298A1 GB 9902427 W GB9902427 W GB 9902427W WO 0006298 A1 WO0006298 A1 WO 0006298A1
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- Prior art keywords
- complex
- support
- functionalised
- group
- metallic
- Prior art date
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- RYZUXXBIKBRCJI-UHFFFAOYSA-N CC(C(OC)=O)Oc1cc(O)cc(CC(OC)=O)c1 Chemical compound CC(C(OC)=O)Oc1cc(O)cc(CC(OC)=O)c1 RYZUXXBIKBRCJI-UHFFFAOYSA-N 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
- C08F8/42—Introducing metal atoms or metal-containing groups
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- 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
- B01J31/165—Polymer immobilised coordination complexes, e.g. organometallic complexes
- B01J31/1658—Polymer immobilised coordination complexes, e.g. organometallic complexes immobilised by covalent linkages, i.e. pendant complexes with optional linking groups, e.g. on Wang or Merrifield resins
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- 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
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
- B01J31/223—At least two oxygen atoms present in one at least bidentate or bridging ligand
- B01J31/2239—Bridging ligands, e.g. OAc in Cr2(OAc)4, Pt4(OAc)8 or dicarboxylate ligands
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- 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
- B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
- B01J2231/32—Addition reactions to C=C or C-C triple bonds
- B01J2231/321—Hydroformylation, metalformylation, carbonylation or hydroaminomethylation
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- 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
- B01J2231/52—Isomerisation reactions
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- 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
- B01J2231/60—Reduction reactions, e.g. hydrogenation
- B01J2231/64—Reductions in general of organic substrates, e.g. hydride reductions or hydrogenations
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- 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
- B01J2231/60—Reduction reactions, e.g. hydrogenation
- B01J2231/64—Reductions in general of organic substrates, e.g. hydride reductions or hydrogenations
- B01J2231/641—Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes
- B01J2231/643—Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes of R2C=O or R2C=NR (R= C, H)
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0213—Complexes without C-metal linkages
- B01J2531/0219—Bimetallic complexes, i.e. comprising one or more units of two metals, with metal-metal bonds but no all-metal (M)n rings, e.g. Cr2(OAc)4
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/82—Metals of the platinum group
- B01J2531/821—Ruthenium
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- 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
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/82—Metals of the platinum group
- B01J2531/822—Rhodium
Definitions
- the invention relates to metallic complexes suitable for attachment to a support, and also to the supported metallic complexes. It also relates to functionalised polymers for use in the preparation of supported metallic complexes.
- a catalyst which is usually an enzyme or a transition metal complex, is added to reactions in order to increase the reaction rate. In some cases, the length of time that a given chemical reaction would be expected to take can be changed from hundreds of years to a few minutes, or even seconds, by the addition of a catalyst.
- Catalysts are typically classified as either homogeneous or heterogeneous. Homogeneous catalysts are those in which the catalyst, reactants and products are all present in the same phase, for example where all species are in solution and there is no particulate solid. With heterogeneous catalysts, the catalyst is in a different phase to the reactants and/or products. Typically, the catalyst is a solid and the reactants and products are liquids or gases or solids dissolved in solution.
- a major objective in the design of new catalysts is to provide for efficient catalyst recovery thus minimising both catalyst cost and reaction product contamination ⁇ Applied Homogeneous Catalysis wi th Organometallic Compounds, B. Cornils and W. A. Herrmann (Eds.), VCH, Weinheim, 1996) .
- it is easy to separate the catalyst from the products for example, by filtration, because the catalyst is usually a solid and the product is usually in a liquid phase.
- reaction product contamination with the catalyst arises where it is difficult or very expensive to remove the catalyst from the product because they are in the same phase.
- the problem occurs commonly in homogeneous catalysis and is the most serious disadvantage of the technique.
- transition metal catalysts based on expensive metals such as rhodium, palladium or platinum
- the issue of cost is a very important factor as even losses in the parts per million range can render the entire process economically unfeasible.
- product contamination must be completely eliminated.
- Dinuclear rhodium (II) complexes are particularly interesting as they are able to catalyse a rich diversity of hydrogenation, carbonylation and cycloalkylation reactions ⁇ Homogeneous Ca talysis wi th Compl exes of Rhodi um and Iridi um, R. S. Dickson, Kluwer Academic Publishers, New York, 1983) . While phosphines are often added to generate a catalytic rhodium (I) species, there is much evidence to suggest that rhodium (II) can also catalyse such chemistry (C. Claver, N. Ruiz, P. Lahuertaand E. Peris, Jnorg. Chim.
- Dirhodium (II) tetraacetate which is obtained as the crystalline solvate 1 (see scheme I below) from methanol, is a particularly convenient source of Rh(II) in that it is easy prepare and air- stable. Its structure is interesting in that the four carboxylate groups form ⁇ -bridges such that each donates one oxygen atom to each of the two metal ions.
- a first object of the invention is a functionalised support for use in the preparation of a supported metallic complex which comprises a polymer backbone bearing at least one functionalised site able to react with and bind to at least one metallic species.
- 'metallic species we mean one or more metal atoms or one or more metal ions (having any possible oxidation state) and also includes such metal atoms and ions in the form of a complex.
- the functionalised site comprises at least two branched groups X and Y, each bearing a functionalised group able to react with and bind to at least one metallic species, and preferably to a bimetallic complex.
- each of the functionalised groups (attached to said X or Y groups) are each able to chelate at least two metallic species and each functionalised group comprises two donor atoms.
- donor is intended to describe atoms having a good ability to transfer electron (s) to other atoms in order to form chemical bonds therewith.
- the X and Y groups are separated by a spacer which is a non-reactive group.
- the spacer is an aromatic ring. While the spacer is preferably a trifunctionalised derivatised benzene ring other trifunctionalised molecules could be used as a substitute, for example, glycerol derivatives.
- a functionalised group Z is attached to said spacer and is the only connection of the spacer and the X and Y groups to the polymer backbone. It is also preferred that the group Z is an heteroatom chosen from the group consisting of oxygen, nitrogen and sulphur to allow easy attachment of the resin material to the ligand-linker . Z could also contain other atoms that connect the spacer of the ligand-linker to the resin material. For example, Z could also be an aromatic hydroxy ethyl or aminomethyl group where, preferably, the heteroatom would be linked to the polymer. However, other types of connection are not excluded.
- the functionalised groups attached to said X and Y groups are carboxylate groups.
- X and Y can be disposed in a meta- or ortho- position relative to each other. The meta- position is preferred.
- X is advantageously chosen from the group consisting of -CH 0-, -CHR-0-, -CH 2 CH 2 - and -CHRCH - .
- Y is advantageously chosen from the group consisting of -CH 2 0-, -CHR-0-, -CH 2 CH 2 - and -CHRCH 2 -.
- An especially preferred functionalised site comprises a bis-carboxylalkylated eta-substituted dihydroxybenzene group.
- Systems based upon bis-carboxyalkylated eta- substituted dihydroxybenzenes, e.g. where X and Y have the structure (-CH 2 0- or -CHR-0-) are particularly preferred because the introduction of the carboxylate moieties into the ligand-linker is easier preparatively.
- the metallic species be one of a transition metal like rhodium or ruthenium.
- the polymer backbone is a Merrifield resin.
- the polymer support may be a Merrifield resin, a modified polytetrafluoroethylene or any other organic polymeric material that would survive the reaction conditions needed to support a given catalytic reaction.
- Another object of the invention is a metallic species attached to a support as described above, and preferably having the structure A shown below.
- a further object of the invention is a method of synthesis of a supported metallic complex, the method comprising the steps of : - reacting under suitable conditions a metallic species with a functionalised support of the invention described above.
- a further object of the invention is a metallic complex comprising at least one metallic atom and a ligand capable of being attached to a polymer support. More particularly the ligand may comprise at least two branched groups X and Y, each bearing a functionalised group which is bound to said metallic atom.
- the functionalised groups attached to both X and Y groups each comprise two donor atoms which chelate at least two metallic atoms.
- said ligand is able to react with and bind to a bimetallic complex.
- the metal preferred is rhodium or ruthenium and it is especially preferred that the functionalised groups attached to said X and Y groups are carboxylate groups.
- Such groups are particularly for binding to dinuclear complexes derived from metal ions and/or metallic complexes like, especially, dirhodium tetraacetate.
- the X and Y groups are disposed in a meta- or ortho- position relative to each other. It is also preferred that X is chosen from the group consisting of -CH 2 0-, -CHR-0-, -CH 2 CH 2 - and -CHRCH 2 - and that Y is chosen from the group consisting of -CH 2 0-, -CHR-0-, -CH CH 2 - and -CHRCH 2 - .
- X and Y groups are separated by a spacer which is a non-reactive group.
- the spacer is preferably an aromatic ring like benzene, and the ligand thus comprises a trifunctionalised derivatised benzene ring.
- the spacer comprises a functionalised group Z' which can easily react with and bind to said polymer support. More particularly the spacer can be aromatic ring and the group Z' may a hydroxyl moiety.
- the connecting group Z (derived from Z' ) is an oxygen atom.
- the group Z may be another heteroatom like nitrogen or sulphur to allow easy attachment of the resin material to the ligand-linker.
- Z could also contain other atoms that connect the third functionalised site of the ligand-linker to the resin material.
- Z could also be an aromatic hydroxymethyl or aminomethyl group where, preferably, the heteroatom would be linked to the polymer and other types of connection are not excluded.
- a particularly preferred ligand comprises a bis- carboxylalkylated meta-substituted dihydroxybenzene group.
- Systems based upon bis-carboxyalkylated meta- substituted dihydroxybenzenes, e.g. where X and Y have the structure (-CH 2 0- or -CHR-0-) are particularly preferred because the introduction of the carboxylate moieties into the ligand-linker is easier preparatively.
- Another object of the invention is a metallic complex attached to a polymer support as described above, and preferably having the structure A shown below.
- the polymer support may be a Merrifield resin, a modified polytetrafluoroethylene or any other organic polymeric material that would survive the reaction conditions needed to support a given catalytic reaction.
- a further object of the invention is a method of synthesis of a supported metallic complex of the invention, said method comprising the step of : reacting under suitable conditions a metallic complex described above with a polymer support.
- a further object of the invention is the use of the metallic complexes described above as catalysts.
- Such catalysed reactions are, for example, hydroformylation, isomerisation and reduction reactions.
- Example A Synthesis of a resin-bounded dirhodium catalyst using dirhodium tetraacetate as starting material and use of the supported catalyst obtained in hydroformylation and isomerisation reactions.
- two of the carboxylate ligands of the dirhodium tetraacetate of structure 1 are replaced by a templated dicarboxylate which positions each carboxyl group in a position similar to adjacent carboxyl groups in the tetraacetate complex of structure 1 (i.e. at approximately 90° one from each other as shown in structure 2) .
- appropriate functionalisation of the dicarboxylate moieties through linker Z allows to anchor the dinuclear metal ion assembly to the polymer via the dicarboxylates, in a form close to the natural structure of corresponding dirhodium tetraacetate complex of structure 1.
- Meta-disubstituted benzenes used in structure 3 are capable of facilitating the formation of two ⁇ -coordinated 11- or 12-membered rings and cause little perturbation to the positions of the other carboxylate groups in dirhodium (II) tetraacetate.
- the methyl esters 5 can be mono O-alkylated with either methyl- or t-butyl- bromoacetic ester and the isolated phenolic diesters 6 are reacted with chloromethylated polystyrene (Merrifield resin) in the presence of sodium hydride (D. Stones, D. J. Miller, M. W. Beaton, T. J. Rutherford and D. Gani, Tetrahedron Lett . , 1998,39, 4875) to give the resin immobilised jbis-carboxylic esters 7. These esters 7 are obtained in quantitative yield from the diesters 6 as judged using a fluorophenol-based gel-phase NMR assay (D. Stones, D. J. Miller, M.
- the resin recovered was a distinctive dark green colour and was isolated in a mass of 136 mg (maximum possible recovery was 151 mg) .
- Spectrometric data : v max (KBr disc) /cm -1 3431m, 3019m,2921s, 2852s, 1945m, 1872m, 1779s, 1739s, 1720m, 1636m, 1597s, 1489s, 1445s, 1342s, 1263s, 1214s, 1136s, 1067s, 1023s, 900m, 836m, 817m and748vs.
- Rhodium in a glass-lined autoclave was added 1 cm of substrate (hex-1-ene) , 4cm 3 of dry, degassed solvent (toluene) and 10 mm 3 (about 3-fold molar excess) of phosphine (PEt 3 ) .
- the autoclave was sealed and pressurised to 40 bar with synthesis gas (1:1 C0:H 2 ) and heated to 80 °C, with stirring. Stirring was continued at this temperature, under pressure, for 10 hours, after which time the autoclave was cooled to 1 room temperature, vented and the reaction products
- the polymer-supported catalyst 3 was also tested for catalytic activity in the isomerisation of hex-1-ene, and after 10 hours at 80 °C, 69% conversion to hex-2- ene was observed.
- Example B Use of supported dirhodium (DIOP) catalyst in the reduction of acetophenone and study of the stereoisomerism of the reaction.
- DIOP dirhodium
- Tests were carried out on the catalytic activity of the resin bound dinuclear rhodium chelated with (-) DIOP (2.3-0-Isopropylidene-2, 3-dihydroxybis (diphenylphosphino) butane) .
- this ligand proceed to attach the ligand (-)DIOP to the metal prior to attachment on the polymer support proved to be the more effective synthetic pathway.
- Such method could also be applied to the synthesis of compounds (3) .
- compound 6 may bet treated with NaOH to cleave the ester protecting group.
- the free diacid thus obtained may be treated with the rhodium tetraacetate complex 1 to synthesis a bimetallic complex of the invention which can eventually be attached to a resin support.
- Rhodium- (-) -DIOP supported resin (19.54 mg, 21.5 ⁇ mol) and potassium hydroxide powder (7.23 mg, 0.129 mmol) were suspended in degassed iso-propanol (5 cm 3 ) under an inert atmosphere and stirred for 15 min.
- Acetophenone 50 mm 3 , 0.43 mmol was added to the solution and the resulting mixture was allowed to stir at 70 °C under inert atmosphere for 19 h.
- Reaction conversions and enantiomeric excesses were determined by gas chromatography using a chiral capillary column CPCHIRASIL-DEX CBTM. Oven conditions : 100 ° c for 3 min ' then 5 ° c P er min - up to 140 °C.
- Carrier gas Helium.
- Example C Use of a dirhodium based chiral-linker catalyst in the reduction of acetophenone and study of the stereoisomerism of the reaction.
- New unsupported dimetallic chiral-linker compounds having a ligand suitable to be attached to a support and having a structure similar to structure A have been studied for their catalyst and their abilities for asymmetric reduction.
- the 3,5- dihydroxyphenylacetate is treated with sodium hydride in tetrahydrofuran and then reacted with the bromoester 13 to give the diester 14 as a pale yellow oil in 36% yield.
- the resulting diester is saponified with sodium hydroxide to give the free diacid 15, which is reacted, without further purification with dirhodium tetracetate in tetrahydrofuran to give the desired chiral support 11 .
- This complex 11 was then tested as chiral catalyst in 2 the reduction of acetophenone, following the same 3 reactional scheme than the one shown in scheme 4. 4 Although, 95% conversion was achieved after 6 h, the 3% 5 enantiomeric excesses (ee) was small. The enantiomeric 6 excesses were determined by gas chromatography using a 7 chiral capillary column CP CHIRASIL-DEXTM as described above .
- (2S)-Alanine 7 (4.0 g, 45 mmol) was added to a saturated solution of potassium bromide (10 cm 3 ), followed by the dropwise addition of hydrogen bromide (15 cm 3 of a48% solution) .
- the resulting mixture was then cooled to 0 °C and sodium nitrite (6.21 g, 90 mmol) was added over 2 h.
- the reaction mixture was maintained below 5 °C for a further 1 hour, and then allowed to warm to room temperature overnight.
- the resulting solution was then extracted with diethyl ether (3x25 cm 3 ) .
- the combined ether extracts were then dried (MgSOzj) and concentrated under reduced pressure to give a pale yellow oil.
- Spectrometric data v max (CHCl 3 )/cm -1 1755 (CO); ⁇ H (300 MHz; CDC1 3 )1.75 (3H, d, J l , CECH 3 ) , 3.72 (3H, s, OCH 3 ) and 4.33 (IH, q, J l , CHCH3) ; ⁇ c (50.3 MHz; CDCI3) 22.5(CH 3 ), 40.2 (CHCH3), 53.3 (OCH 3 ) and 170.5 (COOCH3) .
- the chiral complex (0.0215 mmol) and potassium hydroxide powder (7.23 mg, 0.129 mmol) were dissolved in degassed iso-propanol (5 cm 3 ) under an inert atmosphere and stirred for 15 minutes.
- Acetophenone (50 mm 3 , 0.43 mmol) was then added to the solution, and the resulting mixture was allowed to stir at room temperature under inert atmosphere.
- the conversion rate and the enantiomeric excess (ee) of the mixture is analysed by gas chromatography as described above. The analyse shows a good conversion rate of about 95%, but a poor enantiomeric excess (about 3%) .
- Example D Use of a new diruthenium based chiral- linker catalyst both unsupported and supported in the reduction of acetophenone and study of the stereoisomerism of the reaction.
- the chiral dirutheniu tetraacetate complex 16 was synthesised in an identical manner to that described for the chiral dirhodium tetraacetate complex 11, using the diacid 15 and dirutheniumtetraacetate chloride (R. Mitchell, A. Spencer and G. Wilkinson, J. C. S . Dal ton, 1973, 846.
- the chiral complex (0.0215 mmol) and potassium hydroxide powder (7.23 mg, 0.129 mmol) were dissolved in degassed iso-propanol (5 cm 3 ) under an inert atmosphere and stirred for 15 min.
- Acetophenone (50 mm 3 , 0.43mmol) was then added to the solution, and the resulting mixture was allowed to stir at room temperature under inert atmosphere. After 2 hours the mixture is analysed by chiral gas chromatography : ) .
- the conversion rate was low (about 4%) but the enantiomeric excess was unexpectedly excellent (about 96%) . Therefore the catalyst compound is a particularly preferred embodiment of the invention together with its obvious structural equivalents.
- linker Z' (here an hydroxyl moiety) might be omitted and/or replace by another chemical moiety.
- this ruthenium complex 16 was attached to a resin and then tested as chiral catalyst in the reduction of acetophenone, the conversion rate reached 50% but the enantiomeric excess was surprisingly only 3%.
- these catalysts 11 and 16 attached or unattached should also be effective in the reduction of cinnamate derivatives (A. Corma, M. Iglesias,C. del Pino and F. Sanchez, J. Chem . Soc , Chem. Commun. , 1991, 1253) 17, to give the corresponding chiral ⁇ -amino acids 18 as described in Scheme 7.
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Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP99934971A EP1027155A1 (en) | 1998-07-25 | 1999-07-26 | Metal complexes suitable for attachment to a support and supported metal complexes |
AU50584/99A AU5058499A (en) | 1998-07-25 | 1999-07-26 | Metal complexes suitable for attachment to a support and supported metal complexes |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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GB9816157.3 | 1998-07-25 | ||
GBGB9816157.3A GB9816157D0 (en) | 1998-07-25 | 1998-07-25 | Catalyst |
Publications (1)
Publication Number | Publication Date |
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WO2000006298A1 true WO2000006298A1 (en) | 2000-02-10 |
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ID=10836111
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/GB1999/002427 WO2000006298A1 (en) | 1998-07-25 | 1999-07-26 | Metal complexes suitable for attachment to a support and supported metal complexes |
Country Status (4)
Country | Link |
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EP (1) | EP1027155A1 (en) |
AU (1) | AU5058499A (en) |
GB (1) | GB9816157D0 (en) |
WO (1) | WO2000006298A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002070130A1 (en) * | 2001-03-08 | 2002-09-12 | Merck Patent Gmbh | Catalytically active support |
CZ305277B6 (en) * | 2011-12-08 | 2015-07-15 | Masarykova Univerzita | Catalyst for chemical syntheses based on metal complex and process for preparing thereof |
CN113769780A (en) * | 2021-10-08 | 2021-12-10 | 浙江吉泰新材料股份有限公司 | Magnetic microsphere-loaded bi-acidic ionic liquid catalyst and preparation and application thereof |
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EP0005569A1 (en) * | 1978-05-15 | 1979-11-28 | Shell Internationale Researchmaatschappij B.V. | Resin-ligand-transition metal complex composition and processes for using this composition as catalyst |
US4238358A (en) * | 1977-04-14 | 1980-12-09 | Western Kentucky University | Heterogeneous catalytic hydrogenation |
EP0169161A2 (en) * | 1984-07-17 | 1986-01-22 | The Goodyear Tire & Rubber Company | Polymer bound Fischer-Tropsch catalysts |
EP0405268A2 (en) * | 1989-06-29 | 1991-01-02 | Bayer Ag | Process for the hydrogenation of olefines containing nitrile groups |
WO1994012545A1 (en) * | 1992-11-27 | 1994-06-09 | Naesman Jan H | Process for the preparation of a graft copolymer bound catalyst |
EP0728768A2 (en) * | 1995-02-24 | 1996-08-28 | Ciba-Geigy Ag | Phosphine groups linked to polymer side chains and their metal complexes |
-
1998
- 1998-07-25 GB GBGB9816157.3A patent/GB9816157D0/en not_active Ceased
-
1999
- 1999-07-26 AU AU50584/99A patent/AU5058499A/en not_active Abandoned
- 1999-07-26 WO PCT/GB1999/002427 patent/WO2000006298A1/en not_active Application Discontinuation
- 1999-07-26 EP EP99934971A patent/EP1027155A1/en not_active Withdrawn
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
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GB1408013A (en) * | 1972-12-13 | 1975-10-01 | British Petroleum Co | Transition metal-containing catalysts |
DE2659242A1 (en) * | 1976-12-23 | 1978-06-29 | Geb Hennige Heide Dipl C Brito | Metal chelate complexes of e.g. poly:methacryloyl-acetone(s) - useful as corrosion resistant additives in metal coating compsns. |
US4238358A (en) * | 1977-04-14 | 1980-12-09 | Western Kentucky University | Heterogeneous catalytic hydrogenation |
EP0005569A1 (en) * | 1978-05-15 | 1979-11-28 | Shell Internationale Researchmaatschappij B.V. | Resin-ligand-transition metal complex composition and processes for using this composition as catalyst |
EP0169161A2 (en) * | 1984-07-17 | 1986-01-22 | The Goodyear Tire & Rubber Company | Polymer bound Fischer-Tropsch catalysts |
EP0405268A2 (en) * | 1989-06-29 | 1991-01-02 | Bayer Ag | Process for the hydrogenation of olefines containing nitrile groups |
WO1994012545A1 (en) * | 1992-11-27 | 1994-06-09 | Naesman Jan H | Process for the preparation of a graft copolymer bound catalyst |
EP0728768A2 (en) * | 1995-02-24 | 1996-08-28 | Ciba-Geigy Ag | Phosphine groups linked to polymer side chains and their metal complexes |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2002070130A1 (en) * | 2001-03-08 | 2002-09-12 | Merck Patent Gmbh | Catalytically active support |
CZ305277B6 (en) * | 2011-12-08 | 2015-07-15 | Masarykova Univerzita | Catalyst for chemical syntheses based on metal complex and process for preparing thereof |
CN113769780A (en) * | 2021-10-08 | 2021-12-10 | 浙江吉泰新材料股份有限公司 | Magnetic microsphere-loaded bi-acidic ionic liquid catalyst and preparation and application thereof |
CN113769780B (en) * | 2021-10-08 | 2022-05-03 | 浙江吉泰新材料股份有限公司 | Magnetic microsphere-loaded bi-acidic ionic liquid catalyst and preparation and application thereof |
Also Published As
Publication number | Publication date |
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AU5058499A (en) | 2000-02-21 |
EP1027155A1 (en) | 2000-08-16 |
GB9816157D0 (en) | 1998-09-23 |
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