RU2006116565A - Катализаторы для получения алкиленоксидов, имеющие улучшеную стабильность, эффективность и/или активность - Google Patents
Катализаторы для получения алкиленоксидов, имеющие улучшеную стабильность, эффективность и/или активностьInfo
- Publication number
- RU2006116565A RU2006116565A RU2006116565/04A RU2006116565A RU2006116565A RU 2006116565 A RU2006116565 A RU 2006116565A RU 2006116565/04 A RU2006116565/04 A RU 2006116565/04A RU 2006116565 A RU2006116565 A RU 2006116565A RU 2006116565 A RU2006116565 A RU 2006116565A
- Authority
- RU
- Russia
- Prior art keywords
- catalyst according
- catalyst
- zirconium component
- resistant solid
- zirconium
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims 27
- 230000000694 effects Effects 0.000 title claims 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 14
- 229910052726 zirconium Inorganic materials 0.000 claims 14
- 239000007787 solid Substances 0.000 claims 11
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims 4
- 229910052791 calcium Inorganic materials 0.000 claims 4
- 239000011575 calcium Substances 0.000 claims 4
- 229910052709 silver Inorganic materials 0.000 claims 4
- 239000004332 silver Substances 0.000 claims 4
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 claims 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims 3
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims 3
- 150000001342 alkaline earth metals Chemical class 0.000 claims 3
- 125000002947 alkylene group Chemical group 0.000 claims 3
- 238000005470 impregnation Methods 0.000 claims 3
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 claims 2
- 150000001336 alkenes Chemical class 0.000 claims 2
- 229940043430 calcium compound Drugs 0.000 claims 2
- 150000001674 calcium compounds Chemical class 0.000 claims 2
- 238000006735 epoxidation reaction Methods 0.000 claims 2
- 239000011148 porous material Substances 0.000 claims 2
- 239000012808 vapor phase Substances 0.000 claims 2
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical group C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims 1
- 229910052783 alkali metal Inorganic materials 0.000 claims 1
- 150000001340 alkali metals Chemical class 0.000 claims 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 230000000737 periodic effect Effects 0.000 claims 1
- 229910052702 rhenium Inorganic materials 0.000 claims 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 claims 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/02—Synthesis of the oxirane ring
- C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
- C07D301/04—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen
- C07D301/08—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase
- C07D301/10—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with air or molecular oxygen in the gaseous phase with catalysts containing 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/066—Zirconium or hafnium; Oxides or hydroxides 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
- 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
- B01J23/54—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
- B01J23/66—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
- B01J23/54—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
- B01J23/66—Silver or gold
- B01J23/68—Silver or gold with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/683—Silver or gold with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum or tungsten
- B01J23/686—Silver or gold with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum or tungsten with molybdenum
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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
- B01J23/66—Silver or gold
- B01J23/68—Silver or gold with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/688—Silver or gold with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with manganese, technetium or rhenium
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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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
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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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
- B01J37/0203—Impregnation the impregnation liquid containing organic compounds
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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
- B01J35/612—Surface area less than 10 m2/g
-
- 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
- B01J35/63—Pore volume
- B01J35/635—0.5-1.0 ml/g
-
- 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
- B01J35/64—Pore diameter
- B01J35/657—Pore diameter larger than 1000 nm
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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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
- B01J37/0018—Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
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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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Epoxy Compounds (AREA)
- Catalysts (AREA)
Claims (22)
1. Катализатор для получения алкиленоксида с помощью эпоксидирования алкена в паровой фазе, содержащий нанесенное пропиткой серебро и, по меньшей мере, один промотор для увеличения эффективности на жаропрочный твердый носитель, и указанный носитель содержит количество компонента циркония, достаточное для улучшения, по меньшей мере, одного свойства из активности, эффективности и стабильности катализатора, по сравнению со сходным катализатором, который не содержит компонента циркония, указанный компонент циркония присутствует в носителе по существу в виде силиката циркония.
2. Катализатор по п.1, в котором количество нанесенного пропиткой серебра составляет примерно от 2 до 60% от массы катализатора.
3. Катализатор по п.2, в котором количество нанесенного пропиткой серебра составляет примерно от 5 до 50% от массы катализатора.
4. Катализатор по п.3, в котором количество нанесенного пропиткой серебра составляет примерно от 10 до 40% от массы катализатора.
5. Катализатор по п.1, в котором, по меньшей мере, один из промоторов для повышения эффективности содержит, по меньшей мере, один щелочной металл, щелочноземельный металл и/или оксианион элемента, иного, чем кислород, имеющего атомный номер от 5 до 83 и выбранного из Групп 3b-7b и 3а-7a Периодической таблицы.
6. Катализатор по п.1, в котором, по меньшей мере, один из промоторов для повышения эффективности представляет собой элемент пары окислительно-восстановительных полуреакций.
7. Катализатор по п.5, в котором, по меньшей мере, один из промоторов для повышения эффективности представляет собой компонент рения.
8. Катализатор по п.1, в котором указанный жаропрочный твердый носитель, помимо компонента циркония, включает, по меньшей мере, 95 мас.% альфа-оксида алюминия.
9. Катализатор по п.8, в котором указанный жаропрочный твердый носитель, помимо компонента циркония, содержит менее чем примерно 2000 массовых частей на миллион кальция.
10. Катализатор по п.9, в котором указанный жаропрочный твердый носитель, помимо компонента циркония, содержит менее чем примерно 350 массовых частей на миллион кальция.
11. Катализатор по п.8, в котором указанный жаропрочный твердый носитель, помимо компонента циркония и соединений кальция, содержит менее чем примерно 500 массовых частей на миллион щелочноземельного металла, измеренного как оксид щелочноземельного металла.
12. Катализатор по п.1, в котором указанный жаропрочный твердый носитель, помимо компонента циркония, включает, по меньшей мере, 99 мас.% альфа-оксида алюминия.
13. Катализатор по п.12, в котором указанный жаропрочный твердый носитель, помимо компонента циркония, содержит менее чем примерно 2000 массовых частей на миллион кальция.
14. Катализатор по п.13, в котором указанный жаропрочный твердый носитель, помимо компонента циркония содержит менее чем примерно 350 массовых частей на миллион кальция.
15. Катализатор по п.12, в котором указанный жаропрочный твердый носитель, помимо компонента циркония и соединений кальция, содержит менее чем примерно 500 массовых частей на миллион щелочноземельного металла, измеренного как оксид щелочноземельного металла.
16. Катализатор по п.12, в котором жаропрочный твердый носитель имеет морфологию, содержащую взаимно блокирующиеся пластинки альфа-оксида алюминия.
17. Катализатор по п.1, в котором указанный жаропрочный твердый носитель имеет площадь поверхности, по меньшей мере, примерно 0,5 м2/г, объем пор, по меньшей мере, примерно 0,5 см3/г и медианный диаметр пор в пределах между примерно от 1 до 50 микрон.
18. Катализатор по п.1, в котором компонент циркония содержит примерно от 0,01 до 10,0 мас.% силиката циркония по отношению к общей массе носителя.
19. Катализатор по п.18, в котором компонент циркония содержит примерно от 0,1 до 5,0 мас.% силиката циркония по отношению к общей массе носителя.
20. Катализатор по п.19, в котором компонент циркония содержит примерно от 0,3 до 3,0 мас.% силиката циркония по отношению к общей массе носителя.
21. Применение катализатора по пп.1-20 для получения алкиленоксида с помощью эпоксидирования алкена в паровой фазе.
22. Применение по п.21, в котором указанный алкиленоксид представляет собой этиленоксид.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US51197503P | 2003-10-16 | 2003-10-16 | |
US60/511,975 | 2003-10-16 |
Publications (2)
Publication Number | Publication Date |
---|---|
RU2006116565A true RU2006116565A (ru) | 2007-11-27 |
RU2360735C2 RU2360735C2 (ru) | 2009-07-10 |
Family
ID=34520043
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
RU2006116565/04A RU2360735C2 (ru) | 2003-10-16 | 2004-10-07 | Катализаторы для получения алкиленоксидов, имеющие улучшенную стабильность, эффективность и/или активность |
Country Status (10)
Country | Link |
---|---|
US (5) | US20070111886A1 (ru) |
EP (2) | EP2277622B1 (ru) |
JP (2) | JP4824569B2 (ru) |
CN (3) | CN101767039B (ru) |
AR (1) | AR046294A1 (ru) |
AT (1) | ATE526082T1 (ru) |
CA (1) | CA2541992C (ru) |
RU (1) | RU2360735C2 (ru) |
TW (2) | TWI433720B (ru) |
WO (1) | WO2005039757A1 (ru) |
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US7977274B2 (en) | 2006-09-29 | 2011-07-12 | Sd Lizenzverwertungsgesellschaft Mbh & Co. Kg | Catalyst with bimodal pore size distribution and the use thereof |
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TWI454427B (zh) | 2006-11-01 | 2014-10-01 | Dow Global Technologies Llc | α-氧化鋁之成形多孔體及其製備方法 |
EP2152681B1 (en) * | 2007-05-09 | 2017-03-29 | Shell Internationale Research Maatschappij B.V. | An epoxidation catalyst, a process for preparing the catalyst, and a process for the production of an olefin oxide, a 1,2-diol, a 1,2-diol ether, a 1,2-carbonate, or an alkanolamine |
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CA2541992C (en) | 2013-07-09 |
US20100173771A1 (en) | 2010-07-08 |
TW201039915A (en) | 2010-11-16 |
US8513156B2 (en) | 2013-08-20 |
CN101757914A (zh) | 2010-06-30 |
US20090275763A1 (en) | 2009-11-05 |
JP4778093B2 (ja) | 2011-09-21 |
JP4824569B2 (ja) | 2011-11-30 |
CN1867400A (zh) | 2006-11-22 |
EP2277622A1 (en) | 2011-01-26 |
JP2007508143A (ja) | 2007-04-05 |
CN101767039A (zh) | 2010-07-07 |
TWI365766B (en) | 2012-06-11 |
US20100298128A1 (en) | 2010-11-25 |
US20070111886A1 (en) | 2007-05-17 |
RU2360735C2 (ru) | 2009-07-10 |
TWI433720B (zh) | 2014-04-11 |
CN101767039B (zh) | 2015-04-01 |
WO2005039757A1 (en) | 2005-05-06 |
AR046294A1 (es) | 2005-11-30 |
ATE526082T1 (de) | 2011-10-15 |
US8765630B2 (en) | 2014-07-01 |
CA2541992A1 (en) | 2005-05-06 |
EP2277622B1 (en) | 2013-01-09 |
JP2010149121A (ja) | 2010-07-08 |
US20090291847A1 (en) | 2009-11-26 |
EP1675678B1 (en) | 2011-09-28 |
CN1867400B (zh) | 2010-04-14 |
TW200523022A (en) | 2005-07-16 |
EP1675678A1 (en) | 2006-07-05 |
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