RU2007127670A - Катализатор гидрогенизации - Google Patents
Катализатор гидрогенизации Download PDFInfo
- Publication number
- RU2007127670A RU2007127670A RU2007127670/04A RU2007127670A RU2007127670A RU 2007127670 A RU2007127670 A RU 2007127670A RU 2007127670/04 A RU2007127670/04 A RU 2007127670/04A RU 2007127670 A RU2007127670 A RU 2007127670A RU 2007127670 A RU2007127670 A RU 2007127670A
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- Prior art keywords
- specified
- catalyst
- concentration
- oxide
- palladium
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- 239000003054 catalyst Substances 0.000 title claims 28
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims 25
- 229910052763 palladium Inorganic materials 0.000 claims 11
- 239000000758 substrate Substances 0.000 claims 11
- 229910052741 iridium Inorganic materials 0.000 claims 10
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 claims 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 6
- 150000004645 aluminates Chemical class 0.000 claims 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims 3
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical group [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims 3
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 claims 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims 3
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims 3
- 229910000323 aluminium silicate Inorganic materials 0.000 claims 3
- 229910052788 barium Inorganic materials 0.000 claims 3
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 claims 3
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 claims 3
- 229910000420 cerium oxide Inorganic materials 0.000 claims 3
- 229910000423 chromium oxide Inorganic materials 0.000 claims 3
- 229910052802 copper Inorganic materials 0.000 claims 3
- 239000010949 copper Substances 0.000 claims 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims 3
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims 3
- 229910052737 gold Inorganic materials 0.000 claims 3
- 239000010931 gold Substances 0.000 claims 3
- 238000005984 hydrogenation reaction Methods 0.000 claims 3
- 229910052749 magnesium Inorganic materials 0.000 claims 3
- 239000011777 magnesium Substances 0.000 claims 3
- -1 magnesium aluminate Chemical class 0.000 claims 3
- 239000000395 magnesium oxide Substances 0.000 claims 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims 3
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims 3
- 229910052751 metal Inorganic materials 0.000 claims 3
- 239000002184 metal Substances 0.000 claims 3
- 239000000203 mixture Substances 0.000 claims 3
- 229910052759 nickel Inorganic materials 0.000 claims 3
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 claims 3
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 claims 3
- 229910052709 silver Inorganic materials 0.000 claims 3
- 239000004332 silver Substances 0.000 claims 3
- 239000011135 tin Substances 0.000 claims 3
- 229910052718 tin Inorganic materials 0.000 claims 3
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims 3
- 229910052725 zinc Inorganic materials 0.000 claims 3
- 239000011701 zinc Substances 0.000 claims 3
- 229910001928 zirconium oxide Inorganic materials 0.000 claims 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims 2
- 238000005470 impregnation Methods 0.000 claims 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims 2
- 229910052814 silicon oxide Inorganic materials 0.000 claims 2
- 239000000377 silicon dioxide Substances 0.000 claims 1
Classifications
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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
- 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
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group 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
- 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
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/46—Ruthenium, rhodium, osmium or iridium
- B01J23/468—Iridium
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/148—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound
- C07C7/163—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation
- C07C7/167—Purification; Separation; Use of additives by treatment giving rise to a chemical modification of at least one compound by hydrogenation for removal of compounds containing a triple carbon-to-carbon bond
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds
- C10G45/34—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
- C10G45/36—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/32—Selective hydrogenation of the diolefin or acetylene compounds
- C10G45/34—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used
- C10G45/40—Selective hydrogenation of the diolefin or acetylene compounds characterised by the catalyst used containing platinum group metals or compounds thereof
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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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
- B01J21/04—Alumina
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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
- 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
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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
- 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
- B01J23/50—Silver
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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
- 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
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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
- 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
- B01J23/60—Platinum group metals with zinc, cadmium or mercury
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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
- 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
- B01J23/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead
- B01J23/622—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead
- B01J23/626—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead with tin
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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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
- B01J23/8926—Copper and noble metals
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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
- 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
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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
- 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
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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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Analytical Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Claims (21)
1. Катализатор селективной гидрогенизации ацетилена, содержащий иридий ("Ir"), палладий ("Pd") и промотор ("M") на неорганической подложке, где указанный промотор выбран из группы, состоящей из серебра, золота, меди, цинка, олова и их комбинации, и где указанная неорганическая подложка выбрана из группы, состоящей из оксида алюминия, оксида кремния, алюмосиликата, активированного угля, оксида церия, оксида циркония, алюмохромовой подложки, оксида титана, оксида магния, алюминатов металла, алюмината кальция, алюмината магния, гексаалюмината бария, алюмината никеля и их смесей.
2. Катализатор по п.1, где указанный иридий находится в концентрации от 0,001 до 1,5 вес.%.
3. Катализатор по п.2, где указанный иридий находится в концентрации от 0,01 до 0,06 вес.%.
4. Катализатор по п.1, где указанный палладий находится в концентрации от 0,005 до 0,5 вес.%.
5. Катализатор по п.4, где указанный палладий находится в концентрации от 0,01 до 0,06 вес.%.
6. Катализатор по п.1, где указанный промотор находится в концентрации до 0,5 вес.%.
7. Катализатор по п.6, где указанный промотор находится в концентрации до 0,2 вес.%.
8. Катализатор по п.1, где указанная подложка является оксидом алюминия с удельной поверхностью от 30 до 50 м2/г.
9. Катализатор по п.1, где указанная подложка является оксидом альфа-алюминия.
10. Катализатор селективной гидрогенизации ацетилена, содержащий неорганическую подложку и от 0,001 до 1,5 вес.% иридия ("Ir"), от 0,005 до 0,5 вес.% палладия ("Pd") и до 0,5 вес.% промотора ("M"), причем указанный промотор выбран из группы, состоящей из серебра, золота, меди, цинка, олова и их комбинации.
11. Катализатор по п.10, где указанная подложка выбрана из группы, состоящей из оксида алюминия, оксида кремния, алюмосиликата, активированного угля, оксида церия, оксида циркония, алюмохромовой подложки, оксида титана, оксида магния, алюминатов металла, алюмината кальция, алюмината магния, гексаалюмината бария, алюмината никеля и их смесей.
12. Катализатор по п.11, где указанная подложка является оксидом алюминия с удельной поверхностью от 30 до 50 м2/г.
13. Катализатор по п.11, в котором указанная подложка является оксидом альфа-алюминия.
14. Катализатор по п.10, где указанный иридий, указанный палладий и указанные промоторы осаждены методом пропитки в избытке раствора.
15. Катализатор по п.10, где указанный иридий, указанный палладий и указанные промоторы осаждены методом пропитки по начальной влагоемкости.
16. Катализатор по п.10, где указанный иридий находится в концентрации от 0,01 до 0,06 вес.% и указанный палладий находится в концентрации от 0,01 до 0,06 вес.%.
17. Катализатор для селективной гидрогенизации ацетилена, содержащий иридий ("Ir") и палладий ("Pd") на неорганической подложке, причем указанный палладий находится в пределах первых 250 мкм поверхности подложки катализатора.
18. Катализатор по п.17, где указанный катализатор содержит указанный иридий в концентрации от 0,001 до 1,5 вес.% и указанный катализатор содержит указанный палладий в концентрации от 0,005 до 0,5 вес.%.
19. Катализатор по п.17, содержащий дополнительно до 0,5 вес.% промотора ("M"), выбранного из группы, состоящей из серебра, золота, меди, цинка, олова и их комбинаций.
20. Катализатор по п.19, где указанный катализатор содержит указанный иридий в концентрации от 0,01 до 0,06 вес.% и указанный катализатор содержит указанный палладий в концентрации от 0,01 до 0,06 вес.%, и указанный катализатор содержит указанный промотор в концентрации до 0,2 вес.%.
21. Катализатор по п.17, где указанная подложка выбрана из группы, состоящей из оксида алюминия, оксида кремния, алюмосиликата, активированного угля, оксида церия, оксида циркония, алюмохромовой подложки, оксида титана, оксида магния, алюминатов металла, алюмината кальция, алюмината магния, гексаалюмината бария, алюмината никеля и их смесей.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US64543105P | 2005-01-20 | 2005-01-20 | |
| US60/645,431 | 2005-01-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| RU2007127670A true RU2007127670A (ru) | 2009-02-27 |
Family
ID=36346130
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2007127670/04A RU2007127670A (ru) | 2005-01-20 | 2006-01-19 | Катализатор гидрогенизации |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20060178262A1 (ru) |
| EP (1) | EP1899053A1 (ru) |
| CN (1) | CN101146614A (ru) |
| RU (1) | RU2007127670A (ru) |
| WO (1) | WO2006078926A1 (ru) |
Families Citing this family (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7569511B2 (en) * | 2006-05-05 | 2009-08-04 | Basf Catalysts Llc | Catalyst composition for alcohol steam reforming |
| TWI343360B (en) * | 2007-03-09 | 2011-06-11 | Univ Feng Chia | Method for manufacturing metal-carrying carbonaceous material |
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| CN101433841B (zh) * | 2007-12-13 | 2010-04-14 | 中国石油天然气股份有限公司 | 一种选择性加氢催化剂及其制备方法 |
| US8119558B2 (en) * | 2008-03-14 | 2012-02-21 | Süd-Chemie Inc. | Ultra high temperature shift catalyst with low methanation |
| DE202008017277U1 (de) | 2008-11-30 | 2009-04-30 | Süd-Chemie AG | Katalysatorträger |
| EP2204236A1 (en) | 2008-12-19 | 2010-07-07 | Total Petrochemicals Research Feluy | Catalyst and process for hydrogenation of hydrocarbon feedstocks |
| EP2204235A1 (en) | 2008-12-19 | 2010-07-07 | Total Petrochemicals Research Feluy | Catalyst and process for selective hydrogenation of alkynes and dienes |
| US20100292076A1 (en) * | 2009-05-18 | 2010-11-18 | Sud-Chemie Inc. | Ultra high temperature shift catalyst with low methanation |
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| US8323590B2 (en) | 2010-11-02 | 2012-12-04 | Uop Llc | Water gas shift for acetylene converter feed CO control |
| CN102674413B (zh) * | 2011-03-16 | 2014-04-30 | 中国科学院过程工程研究所 | 一种用于co和h2甲烷化的催化剂及其制备方法 |
| CN102836718B (zh) * | 2011-06-20 | 2014-06-04 | 中国科学院过程工程研究所 | 一种介孔六铝酸盐负载镍基的甲烷化催化剂及其制备方法 |
| CN103071495A (zh) * | 2011-10-26 | 2013-05-01 | 中国石油化工股份有限公司 | 一种含二氧化硅助剂的钯金属催化剂及其应用 |
| CN104588006B (zh) * | 2013-10-31 | 2018-04-03 | 中国科学院大连化学物理研究所 | 一种用于炔烃选择加氢的含钯的合金单原子催化剂 |
| JP6236344B2 (ja) * | 2014-03-31 | 2017-11-22 | Ｊｘｔｇエネルギー株式会社 | 芳香族炭化水素用の水素化触媒、及び環状飽和炭化水素の製造方法 |
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| CN105413707B (zh) * | 2015-10-30 | 2017-10-31 | 南京理工大学 | 用于亚硝基二甲胺还原的双金属Pd‑Ni/CeO2‑TiO2催化剂及其制备方法 |
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| CN111135842B (zh) * | 2019-12-26 | 2022-07-01 | 浙江巨化技术中心有限公司 | 一种用于催化转化八氟环丁烷中杂质的催化剂及其制备方法和应用 |
| CN113769737A (zh) * | 2020-06-10 | 2021-12-10 | 台州学院 | 一种乙炔选择性加氢反应用催化剂及其制备方法与应用 |
| CN114605579B (zh) * | 2020-12-03 | 2023-07-14 | 万华化学集团股份有限公司 | 一种聚丙烯催化剂、一种等规聚丙烯及其制备方法 |
| CN114763392B (zh) * | 2021-01-15 | 2023-07-14 | 万华化学集团股份有限公司 | 一种茂金属负载催化剂及其制备方法、乙烯和α烯烃共聚弹性体的制备方法 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL286390A (ru) * | 1961-12-08 | |||
| US3839192A (en) * | 1970-05-22 | 1974-10-01 | Universal Oil Prod Co | Hydrocarbon conversion with a catalytic composite of palladium, iridium and halogen |
| US3953368A (en) * | 1971-11-01 | 1976-04-27 | Exxon Research And Engineering Co. | Polymetallic cluster compositions useful as hydrocarbon conversion catalysts |
| US4812435A (en) * | 1987-01-12 | 1989-03-14 | Exxon Research And Engineering Company | Polymetallic reforming catalysts and their preparation |
| US5475173A (en) * | 1994-07-19 | 1995-12-12 | Phillips Petroleum Company | Hydrogenation process and catalyst therefor |
| US6127310A (en) * | 1997-02-27 | 2000-10-03 | Phillips Petroleum Company | Palladium containing hydrogenation catalysts |
| DE19959064A1 (de) * | 1999-12-08 | 2001-06-13 | Basf Ag | Trägerkatalysator zur Selektivhydrierung von Alkinen und Dienen |
| US6509292B1 (en) * | 2001-03-30 | 2003-01-21 | Sud-Chemie Inc. | Process for selective hydrogenation of acetylene in an ethylene purification process |
| US6936568B2 (en) * | 2002-06-12 | 2005-08-30 | Sud-Chemie Inc. | Selective hydrogenation catalyst |
| US20040260131A1 (en) * | 2003-06-23 | 2004-12-23 | Chevron Phillips Chemical Company ("Cpchem") | Selective hydrocarbon hydrogenation catalyst and process |
-
2006
- 2006-01-19 US US11/334,824 patent/US20060178262A1/en not_active Abandoned
- 2006-01-19 WO PCT/US2006/002071 patent/WO2006078926A1/en not_active Ceased
- 2006-01-19 RU RU2007127670/04A patent/RU2007127670A/ru not_active Application Discontinuation
- 2006-01-19 EP EP06719047A patent/EP1899053A1/en not_active Withdrawn
- 2006-01-19 CN CNA2006800058383A patent/CN101146614A/zh active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| CN101146614A (zh) | 2008-03-19 |
| US20060178262A1 (en) | 2006-08-10 |
| WO2006078926A1 (en) | 2006-07-27 |
| EP1899053A1 (en) | 2008-03-19 |
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| FA92 | Acknowledgement of application withdrawn (lack of supplementary materials submitted) |
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