EP1094897A1 - Verfahren zur herstellung von schalenkatalysatoren durch cvd-beschichtung - Google Patents
Verfahren zur herstellung von schalenkatalysatoren durch cvd-beschichtungInfo
- Publication number
- EP1094897A1 EP1094897A1 EP99929180A EP99929180A EP1094897A1 EP 1094897 A1 EP1094897 A1 EP 1094897A1 EP 99929180 A EP99929180 A EP 99929180A EP 99929180 A EP99929180 A EP 99929180A EP 1094897 A1 EP1094897 A1 EP 1094897A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- shell
- precursors
- catalysts
- cvd
- hfac
- 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.)
- Withdrawn
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 51
- 238000000034 method Methods 0.000 title claims abstract description 44
- 230000008569 process Effects 0.000 title claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 239000002243 precursor Substances 0.000 claims abstract description 31
- 238000005229 chemical vapour deposition Methods 0.000 claims abstract description 28
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052751 metal Inorganic materials 0.000 claims abstract description 19
- 239000002184 metal Substances 0.000 claims abstract description 19
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 15
- 238000000576 coating method Methods 0.000 claims description 16
- 229910052763 palladium Inorganic materials 0.000 claims description 15
- 229910052737 gold Inorganic materials 0.000 claims description 14
- 239000011248 coating agent Substances 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 11
- 238000006722 reduction reaction Methods 0.000 claims description 10
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 claims description 9
- 102000002322 Egg Proteins Human genes 0.000 claims description 9
- 108010000912 Egg Proteins Proteins 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 7
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 6
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 claims description 5
- CUJRVFIICFDLGR-UHFFFAOYSA-N acetylacetonate Chemical compound CC(=O)[CH-]C(C)=O CUJRVFIICFDLGR-UHFFFAOYSA-N 0.000 claims description 5
- 229910052788 barium Inorganic materials 0.000 claims description 5
- 239000012876 carrier material Substances 0.000 claims description 5
- 150000001875 compounds Chemical class 0.000 claims description 5
- 235000014103 egg white Nutrition 0.000 claims description 5
- 210000000969 egg white Anatomy 0.000 claims description 5
- 150000002739 metals Chemical class 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims description 4
- 239000012190 activator Substances 0.000 claims description 4
- 239000003638 chemical reducing agent Substances 0.000 claims description 4
- 210000003278 egg shell Anatomy 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 229910052793 cadmium Inorganic materials 0.000 claims description 3
- 229910052697 platinum Inorganic materials 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 229910052700 potassium Inorganic materials 0.000 claims description 3
- -1 Al 2 0 3 Inorganic materials 0.000 claims description 2
- 229910052684 Cerium Inorganic materials 0.000 claims description 2
- 229910052581 Si3N4 Inorganic materials 0.000 claims description 2
- 229910052792 caesium Inorganic materials 0.000 claims description 2
- 239000000919 ceramic Substances 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 229910052741 iridium Inorganic materials 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 229910052746 lanthanum Inorganic materials 0.000 claims description 2
- 229910052748 manganese Inorganic materials 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 229910052712 strontium Inorganic materials 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- 229910052726 zirconium Inorganic materials 0.000 claims description 2
- 150000002902 organometallic compounds Chemical class 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 abstract description 10
- 238000006243 chemical reaction Methods 0.000 abstract description 10
- 238000003786 synthesis reaction Methods 0.000 abstract description 9
- 238000005984 hydrogenation reaction Methods 0.000 abstract description 3
- 230000003647 oxidation Effects 0.000 abstract description 3
- 238000007254 oxidation reaction Methods 0.000 abstract description 3
- 238000007210 heterogeneous catalysis Methods 0.000 abstract 1
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 53
- 239000010931 gold Substances 0.000 description 46
- 239000007789 gas Substances 0.000 description 22
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 238000005470 impregnation Methods 0.000 description 15
- 150000003839 salts Chemical class 0.000 description 11
- 239000002245 particle Substances 0.000 description 9
- 239000010970 precious metal Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- 230000009467 reduction Effects 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 6
- 239000012159 carrier gas Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 5
- 239000005977 Ethylene Substances 0.000 description 5
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 4
- 239000012696 Pd precursors Substances 0.000 description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- 239000002105 nanoparticle Substances 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 3
- 239000002585 base Substances 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 2
- FNRVUSGGXYUAJJ-UHFFFAOYSA-N C[Au].CP(C)C Chemical compound C[Au].CP(C)C FNRVUSGGXYUAJJ-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 150000004679 hydroxides Chemical class 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 239000003446 ligand Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 125000002524 organometallic group Chemical group 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 239000012694 precious metal precursor Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000010626 work up procedure Methods 0.000 description 2
- POILWHVDKZOXJZ-ARJAWSKDSA-M (z)-4-oxopent-2-en-2-olate Chemical compound C\C([O-])=C\C(C)=O POILWHVDKZOXJZ-ARJAWSKDSA-M 0.000 description 1
- GVNVAWHJIKLAGL-UHFFFAOYSA-N 2-(cyclohexen-1-yl)cyclohexan-1-one Chemical compound O=C1CCCCC1C1=CCCCC1 GVNVAWHJIKLAGL-UHFFFAOYSA-N 0.000 description 1
- OSDWBNJEKMUWAV-UHFFFAOYSA-N Allyl chloride Chemical compound ClCC=C OSDWBNJEKMUWAV-UHFFFAOYSA-N 0.000 description 1
- 238000004438 BET method Methods 0.000 description 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 101150065749 Churc1 gene Proteins 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 102100038239 Protein Churchill Human genes 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229910010413 TiO 2 Inorganic materials 0.000 description 1
- GEIAQOFPUVMAGM-UHFFFAOYSA-N ZrO Inorganic materials [Zr]=O GEIAQOFPUVMAGM-UHFFFAOYSA-N 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- TWKVUTXHANJYGH-UHFFFAOYSA-L allyl palladium chloride Chemical compound Cl[Pd]CC=C.Cl[Pd]CC=C TWKVUTXHANJYGH-UHFFFAOYSA-L 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 125000000058 cyclopentadienyl group Chemical group C1(=CC=CC1)* 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000000921 elemental analysis Methods 0.000 description 1
- ZSWFCLXCOIISFI-UHFFFAOYSA-N endo-cyclopentadiene Natural products C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- BVRRHCPRDPAYFI-UHFFFAOYSA-M gold(1+);trimethylphosphane;chloride Chemical compound [Au]Cl.CP(C)C BVRRHCPRDPAYFI-UHFFFAOYSA-M 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 238000002488 metal-organic chemical vapour deposition Methods 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- DVSDBMFJEQPWNO-UHFFFAOYSA-N methyllithium Chemical compound C[Li] DVSDBMFJEQPWNO-UHFFFAOYSA-N 0.000 description 1
- 229910003465 moissanite Inorganic materials 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Chemical compound [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000009419 refurbishment Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- JQUZTGJSSQCTPV-UHFFFAOYSA-N sodium;cyclopenta-1,3-diene Chemical compound [Na+].C1C=CC=[C-]1 JQUZTGJSSQCTPV-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0221—Coating of particles
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0238—Impregnation, coating or precipitation via the gaseous phase-sublimation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/04—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides onto unsaturated carbon-to-carbon bonds
- C07C67/05—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides onto unsaturated carbon-to-carbon bonds with oxidation
- C07C67/055—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides onto unsaturated carbon-to-carbon bonds with oxidation in the presence of platinum group metals or their compounds
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/48—Silver or gold
- B01J23/52—Gold
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/58—Platinum group metals with alkali- or alkaline earth metals
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/396—Distribution of the active metal ingredient
- B01J35/397—Egg shell like
Definitions
- the invention relates to a process for the preparation of Pd / Au-containing supported catalysts by CVD (Chemical Vapor Deposition) of evaporable Pd / Au precursors.
- CVD Chemical Vapor Deposition
- the supported catalysts produced in this way can be used for a large number of heterogeneously catalyzed
- VAM vinyl acetate monomer
- the supported catalysts used for this synthesis contain Pd and an alkali element, preferably K. Cd, Au or Ba are used as further additives.
- the metal salts can be applied to the support by impregnation, spraying, vapor deposition, dipping or precipitation.
- GB 1 283 737 discloses the preparation of a noble metal coated catalyst by pre-impregnation of the support with an alkaline solution and saturation with 25-90% water or alcohol. The subsequent impregnation with Pd salts and the reduction of the deposited salts to give the metal
- Shell catalysts whereby the penetration depth of the precious metals should be up to 50% of the pellet radius. It is also known to use shell catalysts by impregnating the support with a solution of Pd / Au salts and with an aqueous base, preferably
- GB 1 521 652 receives the same procedure (pre-impregnation with Pd, Au salts, drying, base precipitation, reduction) shell catalysts of the egg white type, ie only an inner ring of the spherical SiO 2 carrier contains the noble metals, while the inner core and a thin outer shell remains almost free of precious metals.
- No. 4,048,096 falls water-insoluble Pd and Au compounds on the support pre-impregnated with Pd / Au salts with Na silicates in portions of NaOH.
- the shell thickness is less than 0.5 mm.
- US Pat. No. 5,185,308 likewise fixes the noble metals in the shell with Na metasilicate or NaOH, in contrast to US Pat. No. 4,048,096 a higher Au / Pd ratio in the range from 0.6 to 1.25 being selected.
- EP 0 51 9 435 discloses the production of a Pd / Au / K or Pd / Cd / K shell catalyst, a special support material being washed with an acid before impregnation and treated with a base after impregnation.
- US Pat. No. 4,087,622 describes the preparation of coated catalysts by pre-seeding with (reduced) Pd / Au metal nuclei in a low concentration, by impregnating the porous SiO 2 or Al 2 O 3 support with a Pd / Au salt solution, is dried and then the Pd / Au salt is reduced to the metal.
- This prenucleation step is followed by the separation of the catalytically necessary amount of noble metal, i.e. the main amount, which then accumulates in a shell near the surface.
- the CVD (Chemical Vapor Deposition) process is as
- This process is mainly used in the production of functional parts
- Materials such as optical fibers, insulators, semiconductors, conductor tracks and hard material layers are used.
- Chemical vapor deposition is one of the most important processes in thin-film technology. Molecular precursors (precursors) transported in the gas phase react to coatings adhering to hot surfaces in the reactor. Gas phase methods that differ from the
- Egg-shell refers to an outer shell that is different from the outer one
- Egg-white is an "inner ring-shaped shell" in a zone of the molded body near the surface, slightly below the outer edge, the very outer zone not covered with precious metals being intended to trap catalyst poisons and thus the catalytically active layers below
- the type of shell and shell thickness (penetration depth of the precious metal precursors) can be influenced experimentally, e.g. about the pressure.
- coated catalysts described in the prior art are produced by impregnation, impregnation, immersion or spray impregnation. CVD has not yet been used.
- noble metal shell catalysts having a defined shell thickness on porous ceramic supports can be coated by coating the support material with undecomposable evaporable Edeimetal precursors
- the precious metals are fixed by simultaneous or subsequent thermal or chemical reduction.
- Suitable as (noble metal) precursors ie active metal compounds which can be concentrated in the shell, are all compounds of the metals which can be evaporated without decomposition, including their mixtures.
- Pd, Au, Pt, Ag, Rh, Ru, Cu, Ir, Ni and / or Co. are preferred.
- Pd, Pt, Ag, Rh and Au are particularly preferred, in particular Pd and Au.
- Suitable Pd precursors are, for example, Pd (allyl) 2 , Pd (C 4 H 7 ) acac, Pd (CH 3 allyl) 2 , Pd (hfac) 2 , Pd (hfac) (C 3 H 5 ), Pd (C 4 H 7 ) (hfac) and PdCp (allyl), in particular PdCp (allyl).
- acac acetylacetonate
- hfac hexaflouracetylacetonate
- Cp cyclopentadienyl
- tfac triflouracetylacetonate
- Me methyl
- Suitable Au precursors include Me 2 Au (hfac), Me 2 Au (tfac), Me 2 Au (acac), Me 3 Au (PMe 3 ), CF 3 Au (PMe 3 ), (CF 3 ) 3 Au ( PMe 3 ), MeAuP (OMe) 2 Bu ⁇ MeAuP (OMe) 2 Me and MeAu (PMe 3 ).
- Me 3 PAuMe is preferred.
- the precious metals are fixed on the carrier by thermal or chemical reduction, subsequently or simultaneously during the coating.
- the process according to the invention it is possible to use shell catalysts with a substantially better metal dispersion and uniformity, i.e. to produce an essentially monomodal and narrow-band particle size distribution, and with smaller particle sizes.
- the average particle diameter of the nanoparticles is usually in the range from 1 nm to 100 nm.
- the shell thickness can be controlled via the CVD process parameters and easily adapted to the catalytic requirements.
- the method according to the invention permits the residue-free fixing of nanoparticles on the carrier material.
- the two noble metals are only distributed in a zone near the surface, while the regions of the shaped support body lying further in are almost are free of precious metals.
- the layer thickness of these catalytically active shells is approximately 5 ⁇ m to 10 mm, in particular 10 ⁇ m to 5 mm, particularly preferably 20 ⁇ m to 3 mm.
- Suitable refurbishments are e.g. in US-A-5,066,365, DE-A-34 22 575, DE-A-34 08 239, DE-A-29 45 91 3, DE-A-26 1 0 624, US-A-3 840 590. If, on the other hand, the plant capacity is kept constant, the reaction temperature can be reduced and the reaction can be carried out more selectively with the same total output, saving educts. At the same time, the amount of carbon dioxide formed as a by-product and therefore to be discharged and the loss of entrained ethylene associated with this discharge are reduced. In addition, this procedure leads to an extension of the catalyst life.
- the noble metal coating and carrier fixation can also be carried out simultaneously in one step, for example by using a reducing agent such as H 2 as carrier gas and / or by maintaining the carrier at an elevated temperature, so that the noble metal precursors immediately after they have been acted on reduced to the carrier surface and thereby fixed.
- a reducing agent such as H 2 as carrier gas and / or by maintaining the carrier at an elevated temperature, so that the noble metal precursors immediately after they have been acted on reduced to the carrier surface and thereby fixed.
- the coating of the carrier material by means of the CVD method is usually carried out in a pressure range from 1 0 '-760 Torr and at a temperature of the furnace in the range of 20-600 ° C and 00 ° C 20-1 of the reservoir.
- the following parameters are preferred for CpPd (allyl):
- Inert materials such as SiO 2 , Al 2 O 3 , TiO 2 , ZrO 2 , MgO, their mixed oxides or mixtures of these oxides, SiC, Si3N4, C, in the form of spheres, tablets, rings, stars or other shaped bodies can be used as carriers become.
- the diameter or the length and thickness of the carrier particles is generally 3 to 9 mm.
- the surface area of the supports, measured using the BET method, is generally 10-500 m 2 / g, preferably 20-250 m 2 / g.
- the pore volume is generally 0.3 to 1.2 ml / g.
- Pd / Au shell catalysts which additionally contain alkali acetates, preferably K-, have proven to be particularly suitable for the vinyl acetate synthesis.
- Activators can be applied to the carrier before and / or after the CVD coating with (Pd / Au) precursors.
- promoters or activators e.g. Compounds of Cd, Ba, Sr, Cu, Fe, Co, Ni, Zr, Ti, Mn, La or Ce can be used.
- the support is first coated with Pd and optionally Au precursors by means of CVD in a zone (shell) close to the surface, the precious metal precursors are reduced to the metals, and optionally with alkali metal or alkaline earth metal acetates, in particular Na, K, Cs or Ba acetate impregnated wet-chemically, the alkali or alkaline earth metal being evenly distributed over the pellet cross section.
- the precious metal precursors are reduced to the metals, and optionally with alkali metal or alkaline earth metal acetates, in particular Na, K, Cs or Ba acetate impregnated wet-chemically, the alkali or alkaline earth metal being evenly distributed over the pellet cross section.
- VAM vinyl acetate monomer
- the Pd content of the Pd / Au / K catalysts is generally 0.5 to 2.0% by weight, preferably 0.6 to 1.5% by weight.
- the K content is generally 0.5 to 4.0% by weight, preferably 1.5 to 3.0% by weight.
- the Au content of the Pd / K / Au catalysts is generally 0.2 to 1.0% by weight, preferably 0.3 to 0.8% by weight.
- At least one precursor must be applied from each of the elements (Pd / Au / K) to be applied to the carrier parts. Multiple precursors can be applied to each element, but generally one salt is applied to each of the three elements. The necessary loads can be applied in one step or by multiple deposition.
- alloys or structured nanostructures ie gold on palladium or palladium on gold, can be produced using the method according to the invention become.
- the Pd and Au precursors can be applied simultaneously or in succession.
- the CVD technology can also be used with the classic
- Impregnation technology can be combined, e.g. only Pd is evaporated, while before and / or after the Pd coating is impregnated with Au salts.
- the CVD process parameters such as the type and partial pressure of the carrier gas, partial pressure of the precursors, admixing of further inert or diluent gases, contact time, temperature etc. allow simple control and controllability of the shell thickness, which can thus be optimally adapted to the requirements.
- smaller shell thicknesses are possible than with impregnation technology, the lower limit of which is approximately 0.5 mm.
- the coating can be controlled in such a way that shell structures of the egg-shell or egg-white type can be produced.
- an inert or reactive carrier gas is usually used to transport the precursors into the coating chamber. If the vapor pressure of the precursors or vacuum is sufficient, the carrier gas can also be dispensed with and the partial pressure of the precursors can be regulated via the evaporation temperature in the storage vessel.
- the meticulously clean equipment and solvents (bidistilled water) that are often required for the preparation of the impregnation solutions are completely eliminated with the CVD technique. Impurities in solvents often lead to undesired agglomeration of particles and can even act as a catalyst poison.
- the supported catalysts produced in this way can be used for a large number of heterogeneously catalyzed reactions such as hydrogenations and oxidations.
- Pd / Au shell catalysts produced by this method can be used according to the invention in vinyl acetate synthesis.
- the invention Compared to the technically used method of precipitating noble metal hydroxides with NaOH followed by a reduction step, the invention has the additional advantage of enormous time savings (and thus cost savings) during production: because according to the invention, the shell can be produced in a few minutes while the NaOH precipitation takes place extends over more than 20 h.
- the subsequent reduction step conventionally still required can be omitted in the method according to the invention, since the formation of the shell structure and the reduction to the metals can take place simultaneously in one step.
- the vinyl acetate is generally prepared by passing over gases containing acetic acid, ethylene and oxygen or oxygen at temperatures of 1 00 to 220 ° C, preferably 1 20 to 200 ° C, and at pressures of 1 to 25 bar, preferably 1 to 20 bar, over the finished catalyst, whereby unreacted components can be circulated.
- the oxygen concentration is expediently kept below 10% by volume (based on the gas mixture free of acetic acid).
- inert gases such as nitrogen or carbon dioxide may also be advantageous.
- Carbon dioxide is particularly suitable for dilution, since it is formed in small quantities during the reaction. Selectivities of 90% and more are achieved with the method according to the invention.
- coated catalysts according to the invention are notable for high activity and selectivity due to their significantly improved metal dispersion and uniformity and significantly reduced particle sizes with larger active metal surfaces.
- Example 3 CVD of the precursors on porous SiO 2 siliperl support balls
- the carrier was germinated with a small amount of Pd precursor, then the Au precursor was evaporated and then the remaining Pd precursor was repeatedly evaporated.
- the carrier gas flow was 0.7 cm 3 / min.
- the sample was analyzed with TEM-EDX and REM-EDX.
- Example 4 Assembling a technical VAM catalyst The Pd / Au-loaded SiO 2 siliperl carrier balls from Example 3 are
- the catalysts produced in the examples are tested in a microfixed bed tube reactor with a fill volume of 36 ml.
- Gas is dosed via mass flow controller (mass flow controller for gases) and acetic acid is dosed with a liquid flow controller (mass flow controller for liquids) (Bronkhorst).
- the gases and the acetic acid are mixed in a gas mixing tube charged with packing.
- the reactor discharge is depressurized to normal pressure and passed through a glass cooler.
- the condensate collected is analyzed off-line with GC.
- the non-condensable gases are quantified by on-line GC.
- the catalyst in the reactor is activated as follows:
- the catalyst is heated under N 2 at normal pressure from approx. 25 ° C to 1 55 ° C.
- the gas temperature increases to 1,50 ° C and the gas mixing temperature
- the catalyst After activation, the catalyst is started up and measured as follows: oxygen is added after the gas mixing tube and the
- the reaction is continuously monitored with the gas chromatograph.
- Sampling begins when the reaction is uniform, ie at a constant reactor temperature and at a constant concentration of vinyl acetate and CO 2 in the product gas stream.
- a liquid sample and several gas samples are taken over a period of approx. 1 h.
- the product gas flow is determined with a gas meter.
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- Materials Engineering (AREA)
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- Catalysts (AREA)
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Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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DE19827844 | 1998-06-23 | ||
DE19827844A DE19827844A1 (de) | 1998-06-23 | 1998-06-23 | Verfahren zur Herstellung von Schalenkatalysatoren durch CVD-Beschichtung |
PCT/EP1999/004031 WO1999067022A1 (de) | 1998-06-23 | 1999-06-11 | Verfahren zur herstellung von schalenkatalysatoren durch cvd-beschichtung |
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EP1094897A1 true EP1094897A1 (de) | 2001-05-02 |
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EP99929180A Withdrawn EP1094897A1 (de) | 1998-06-23 | 1999-06-11 | Verfahren zur herstellung von schalenkatalysatoren durch cvd-beschichtung |
Country Status (7)
Country | Link |
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US (1) | US20010048970A1 (ja) |
EP (1) | EP1094897A1 (ja) |
JP (1) | JP2002518173A (ja) |
CN (1) | CN1306459A (ja) |
CA (1) | CA2336026A1 (ja) |
DE (1) | DE19827844A1 (ja) |
WO (1) | WO1999067022A1 (ja) |
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ES2268635T3 (es) * | 2003-03-03 | 2007-03-16 | Dechema Gesellschaft Fur Chemische Technik Und Biotechnologie E.V. | Procedimiento para recubrir un sustrato. |
FI119588B (fi) | 2003-11-27 | 2009-01-15 | Neste Oil Oyj | Jalometallikatalyytti hiilivetyjen konversiota varten, menetelmä sen valmistamiseksi ja menetelmä dieselpolttoaineen valmistamiseksi |
TW201236755A (en) * | 2003-12-19 | 2012-09-16 | Celanese Int Corp | Halide free precursors for catalysts |
AR056250A1 (es) * | 2003-12-19 | 2007-10-03 | Celanese Int Corp | Metodos para la preparacion de alquenil alcanoatos |
DE102004011335A1 (de) * | 2004-03-09 | 2005-09-22 | Süd-Chemie AG | Präparation von Metall/Metalloxid-Trägerkatalysatoren durch präkursorchemische Nanometallurgie in definierten Reaktionsräumen poröser Träger mittels metallorganischer und/oder anorganischer Präkursoren und metallhaltiger Reduktionsmittel |
FR2872061B1 (fr) * | 2004-06-23 | 2007-04-27 | Toulouse Inst Nat Polytech | Composition solide divisee formee de grains a depot metallique atomique continu et son procede d'obtention |
ZA200704864B (en) * | 2004-12-20 | 2008-08-27 | Celanese Int Corp | Modified support materials for catalysts |
US8227369B2 (en) | 2005-05-25 | 2012-07-24 | Celanese International Corp. | Layered composition and processes for preparing and using the composition |
US7390869B2 (en) * | 2005-06-13 | 2008-06-24 | Eastman Chemical Company | Process for removing metal species in the presence of hydrogen and a porous material and polyester polymer containing reduced amounts of metal species |
DE102005029200A1 (de) | 2005-06-22 | 2006-12-28 | Basf Ag | Katalysator und Verfahren zur Hydrierung von hydrierbare Gruppen enthaltenden organischen Verbindungen |
US20070105713A1 (en) * | 2005-11-10 | 2007-05-10 | Intevep, S.A. | Hydrogenation catalyst with improved textural properties |
JP5582700B2 (ja) * | 2006-09-29 | 2014-09-03 | 株式会社キャタラー | ロジウム担持用薬液及び当該薬液を用いて調製したロジウム触媒 |
JP5142258B2 (ja) * | 2007-02-06 | 2013-02-13 | 独立行政法人産業技術総合研究所 | 炭素担持貴金属ナノ粒子触媒の製造方法 |
DE102007025442B4 (de) | 2007-05-31 | 2023-03-02 | Clariant International Ltd. | Verwendung einer Vorrichtung zur Herstellung eines Schalenkatalysators und Schalenkatalysator |
DE102007025443A1 (de) * | 2007-05-31 | 2008-12-04 | Süd-Chemie AG | Pd/Au-Schalenkatalysator enthaltend HfO2, Verfahren zu dessen Herstellung sowie dessen Verwendung |
DE102007025362A1 (de) | 2007-05-31 | 2008-12-11 | Süd-Chemie AG | Dotierter Pd/Au-Schalenkatalysator, Verfahren zu dessen Herstellung sowie dessen Verwendung |
DE102007025223A1 (de) | 2007-05-31 | 2008-12-04 | Süd-Chemie AG | Zirkoniumoxid-dotierter VAM-Schalenkatalysator, Verfahren zu dessen Herstellung sowie dessen Verwendung |
FR2919309B1 (fr) * | 2007-07-25 | 2011-07-22 | Commissariat Energie Atomique | Procede et dispositif d'infiltration d'une structure en materiau poreux par depot chimique en phase vapeur. |
DE102007047430A1 (de) * | 2007-10-04 | 2009-04-09 | Evonik Degussa Gmbh | Katalysator |
WO2010052672A2 (en) * | 2008-11-07 | 2010-05-14 | L'air Liquide-Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Allyl-containing precursors for the deposition of metal-containing films |
TW201024312A (en) * | 2008-11-07 | 2010-07-01 | Air Liquide | Allyl-containing precursors for the depostion of metal-containing films |
DE202008017277U1 (de) | 2008-11-30 | 2009-04-30 | Süd-Chemie AG | Katalysatorträger |
US8211821B2 (en) | 2010-02-01 | 2012-07-03 | Celanese International Corporation | Processes for making tin-containing catalysts |
DE102010026462A1 (de) * | 2010-07-08 | 2012-01-12 | Süd-Chemie AG | Verfahren zur Herstellung eines Schalenkatalysators und Schalenkatalysator |
CN102764651B (zh) * | 2011-05-06 | 2015-09-23 | 中国石油化工股份有限公司 | 一种制备壳层催化剂的方法和壳层催化剂 |
CN102861575B (zh) * | 2011-07-07 | 2015-07-01 | 中国石油化工股份有限公司 | 一种壳层催化剂及其制备方法 |
US9650711B2 (en) * | 2011-09-26 | 2017-05-16 | California Institute Of Technology, Office Of Technology Transfer | Efficient and simple method for metalorganic chemical vapor deposition |
DE102012003232A1 (de) * | 2012-02-20 | 2013-08-22 | Clariant Produkte (Deutschland) Gmbh | Nachvergoldung von Pd-Au-gecoateten Schalenkatalysatoren |
DE102012003236A1 (de) | 2012-02-20 | 2013-08-22 | Clariant Produkte (Deutschland) Gmbh | Vorvergoldung von Pd-Au-gecoateten Schalenkatalysatoren |
CN104582838A (zh) | 2012-07-02 | 2015-04-29 | 巴斯夫公司 | 用于制备乙酸乙烯酯单体的方法和催化剂复合物 |
WO2014124452A1 (en) * | 2013-02-11 | 2014-08-14 | Stc.Unm | Catalysts with active support |
KR101549641B1 (ko) * | 2013-10-18 | 2015-09-03 | 한국에너지기술연구원 | 감압 잔사유 열분해용 촉매, 이의 제조방법 및 이를 위한 장치 |
CN104549517B (zh) * | 2013-10-28 | 2017-02-15 | 中国石油化工股份有限公司 | 醋酸乙烯催化剂及其应用 |
CN103933974B (zh) * | 2014-05-05 | 2015-05-20 | 中国石油大学(华东) | 负载型钯催化剂的制备方法 |
CN104437477A (zh) * | 2014-11-20 | 2015-03-25 | 西安近代化学研究所 | 一种小尺度、高分散Pd/C催化剂的气相合成方法 |
CN105032430B (zh) * | 2015-08-05 | 2017-09-19 | 万华化学集团股份有限公司 | 一种蛋壳型Co‑Ni‑Fe@SiO2催化剂的制备方法及制备的催化剂及其应用 |
FR3065887B1 (fr) * | 2017-05-04 | 2020-05-15 | IFP Energies Nouvelles | Procede d'addition d'un compose organique a un solide poreux en phase gazeuse |
CN110841705B (zh) * | 2019-11-29 | 2022-09-16 | 万华化学集团股份有限公司 | 一种多孔材料负载高分散纳米铜催化剂及其制备方法与应用 |
CN114345369B (zh) * | 2022-01-12 | 2023-05-30 | 万华化学集团股份有限公司 | 一种乙酰氧化催化剂、其制备方法及制备醋酸烯酯的方法 |
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US5179056A (en) * | 1991-05-06 | 1993-01-12 | Union Carbide Chemicals & Plastics Technology Corporation | Production of alkenyl alkanoate catalysts |
DE4221011A1 (de) * | 1992-06-26 | 1994-01-05 | Basf Ag | Schalenkatalysatoren |
JPH06165936A (ja) * | 1992-09-03 | 1994-06-14 | Chisso Corp | アルミナ担持白金触媒 |
JP2814445B2 (ja) * | 1992-09-16 | 1998-10-22 | インターナショナル・ビジネス・マシーンズ・コーポレイション | 選択的な金の低温化学蒸着 |
DE4333293A1 (de) * | 1993-09-30 | 1995-04-06 | Basf Ag | Verfahren zur selektiven Hydrierung von Butindiol-1,4 zu Buten-2-diol-1,4 und dafür geeigneter Katalysator |
-
1998
- 1998-06-23 DE DE19827844A patent/DE19827844A1/de not_active Withdrawn
-
1999
- 1999-06-11 CN CN99807726A patent/CN1306459A/zh active Pending
- 1999-06-11 CA CA002336026A patent/CA2336026A1/en not_active Abandoned
- 1999-06-11 JP JP2000555699A patent/JP2002518173A/ja active Pending
- 1999-06-11 WO PCT/EP1999/004031 patent/WO1999067022A1/de not_active Application Discontinuation
- 1999-06-11 EP EP99929180A patent/EP1094897A1/de not_active Withdrawn
-
2000
- 2000-12-18 US US09/739,061 patent/US20010048970A1/en not_active Abandoned
Non-Patent Citations (1)
Title |
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See references of WO9967022A1 * |
Also Published As
Publication number | Publication date |
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WO1999067022A1 (de) | 1999-12-29 |
CN1306459A (zh) | 2001-08-01 |
JP2002518173A (ja) | 2002-06-25 |
CA2336026A1 (en) | 1999-12-29 |
US20010048970A1 (en) | 2001-12-06 |
DE19827844A1 (de) | 1999-12-30 |
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