WO2008019585A1 - Procédé de modification d'un tamis moléculaire à micropores de silicoaluminium phosphate au moyen d'un métal - Google Patents
Procédé de modification d'un tamis moléculaire à micropores de silicoaluminium phosphate au moyen d'un métal Download PDFInfo
- Publication number
- WO2008019585A1 WO2008019585A1 PCT/CN2007/002349 CN2007002349W WO2008019585A1 WO 2008019585 A1 WO2008019585 A1 WO 2008019585A1 CN 2007002349 W CN2007002349 W CN 2007002349W WO 2008019585 A1 WO2008019585 A1 WO 2008019585A1
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- WO
- WIPO (PCT)
- Prior art keywords
- molecular sieve
- modified
- metal
- sap0
- sapo
- Prior art date
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- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 71
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 58
- 238000000034 method Methods 0.000 title claims abstract description 23
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 22
- 239000002184 metal Substances 0.000 title claims abstract description 22
- 229910019142 PO4 Inorganic materials 0.000 title abstract 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 title abstract 3
- 239000010452 phosphate Substances 0.000 title abstract 3
- 239000000843 powder Substances 0.000 claims abstract description 19
- 239000003054 catalyst Substances 0.000 claims abstract description 16
- 238000000227 grinding Methods 0.000 claims abstract description 10
- -1 SAPO-34 Chemical compound 0.000 claims abstract description 8
- 229910052712 strontium Inorganic materials 0.000 claims abstract description 8
- 229910052788 barium Inorganic materials 0.000 claims abstract description 7
- 150000001875 compounds Chemical class 0.000 claims abstract description 7
- 229910052802 copper Inorganic materials 0.000 claims abstract description 7
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 7
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 6
- 229910052723 transition metal Inorganic materials 0.000 claims abstract description 5
- 150000003624 transition metals Chemical class 0.000 claims abstract description 5
- 150000002739 metals Chemical class 0.000 claims abstract description 4
- 239000011148 porous material Substances 0.000 claims description 22
- 239000000203 mixture Substances 0.000 claims description 13
- 150000003839 salts Chemical class 0.000 claims description 8
- 239000011701 zinc Substances 0.000 claims description 8
- 239000010949 copper Substances 0.000 claims description 7
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 6
- 238000002715 modification method Methods 0.000 claims description 6
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical class [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 claims description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical class [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 5
- 229910052783 alkali metal Inorganic materials 0.000 claims description 5
- 150000001340 alkali metals Chemical class 0.000 claims description 5
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical class [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 claims description 5
- 239000011575 calcium Substances 0.000 claims description 5
- 238000005470 impregnation Methods 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 3
- 229910021645 metal ion Inorganic materials 0.000 claims description 3
- 239000012266 salt solution Substances 0.000 claims description 3
- 238000007598 dipping method Methods 0.000 claims description 2
- 229910017053 inorganic salt Inorganic materials 0.000 claims description 2
- 230000002194 synthesizing effect Effects 0.000 claims 1
- 150000001336 alkenes Chemical class 0.000 abstract description 9
- 229910052799 carbon Inorganic materials 0.000 abstract description 6
- 238000002156 mixing Methods 0.000 abstract description 4
- 238000007654 immersion Methods 0.000 abstract description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 27
- 238000006243 chemical reaction Methods 0.000 description 10
- 241000269350 Anura Species 0.000 description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000003837 high-temperature calcination Methods 0.000 description 2
- 238000001027 hydrothermal synthesis Methods 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical group [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical group 0.000 description 1
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- UNYSKUBLZGJSLV-UHFFFAOYSA-L calcium;1,3,5,2,4,6$l^{2}-trioxadisilaluminane 2,4-dioxide;dihydroxide;hexahydrate Chemical compound O.O.O.O.O.O.[OH-].[OH-].[Ca+2].O=[Si]1O[Al]O[Si](=O)O1.O=[Si]1O[Al]O[Si](=O)O1 UNYSKUBLZGJSLV-UHFFFAOYSA-L 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 229910052676 chabazite Inorganic materials 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910052675 erionite Inorganic materials 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 125000001145 hydrido group Chemical group *[H] 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 150000002927 oxygen compounds Chemical class 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001308 synthesis method 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/82—Phosphates
- B01J29/84—Aluminophosphates containing other elements, e.g. metals, boron
- B01J29/85—Silicoaluminophosphates [SAPO compounds]
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/54—Phosphates, e.g. APO or SAPO compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/12—After treatment, characterised by the effect to be obtained to alter the outside of the crystallites, e.g. selectivation
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/20—After treatment, characterised by the effect to be obtained to introduce other elements in the catalyst composition comprising the molecular sieve, but not specially in or on the molecular sieve itself
-
- 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
- B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
-
- 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
- B01J23/06—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of zinc, cadmium or mercury
-
- 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
- B01J23/72—Copper
-
- 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
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/78—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali- or alkaline earth metals
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2529/00—Catalysts comprising molecular sieves
- C07C2529/82—Phosphates
- C07C2529/84—Aluminophosphates containing other elements, e.g. metals, boron
- C07C2529/85—Silicoaluminophosphates (SAPO compounds)
Definitions
- the invention relates to a metal modification method of a small pore phosphorus silicon aluminum molecular sieve, and a catalytic application of a metal modified molecular sieve catalyst in the reaction of converting oxygen compounds into low carbon olefins.
- Low-carbon olefins are the basic raw materials for petrochemicals. With the development of the world economy, its demand is increasing year by year. The main route for the production of ethylene and propylene is currently through naphtha cracking. Because petroleum is a non-renewable resource with limited reserves, research and development of new low-carbon olefin production technologies is of great significance. Natural gas or coal by methanol The production of low-carbon olefins such as ethylene and propylene is the most promising alternative to the naphtha route to olefins.
- SAPO-n phosphosilicate series molecular sieve
- SAPO molecular sieves are a class of crystalline silicoaluminophosphates composed of tetrahedrons of P0 4 +, A10 4 — and Si0 4 .
- SAPO molecular sieves with small pores and moderate acidity have been used for MTO reactions such as SAPO-17, SAPO-18, SAPO-34, SAPO-44, etc.
- US4499327 their pore sizes are approximately It is a good type of shape-selective catalyst with 0.43nm.
- SAPO-34 molecular sieve has become a hot spot in MTO reaction due to its suitable acidity and pore structure.
- CN1167654A discloses the modification of SAPO-34 by using Cu, Co, Ni, Ca, Ba or Sr, and adding a binder and a pore former to prepare a catalyst for converting methanol or dimethyl ether into a lower olefin.
- the metal is introduced into the SAPO-34 molecular sieve by direct in situ synthesis or impregnation, and the mass of the metal in the molecular sieve is 0.01-0.15%.
- CN1216941A reports the use of calcium, strontium and barium and mixtures thereof to modify small pore molecular sieves and their use in the conversion of oxygenates.
- the modification method of the molecular sieve of the patent is divided into two types, one is direct in-situ synthesis, and the other is to modify the synthesized molecular sieve raw powder by the impregnation method.
- US4752651 Non-zeolite small pore molecular sieves have been reported to be modified with alkaline earth metals strontium and magnesium.
- JP 940 74 134 discloses a process for alkaline earth metal modified molecular sieves which refers to a molecular sieve pore size between macroporous zeolites such as X and Y zeolites and small pore molecular sieves such as erionite and chabazite.
- US2004224839 reports a process for modifying calcined SAPO molecular sieves such as SAPO-34 using organometallic reagents. Summary of the invention
- the technical solution of the present invention is to provide a metal modification method for a small-porous phosphosilica molecular sieve, which comprises impregnating or mechanically grinding a compound containing an alkali metal and/or a transition metal with a small hole.
- the original powder of the phosphorus silicon aluminum molecular sieve is mixed to prepare a modified molecular sieve.
- the small pore phosphosilica molecular sieve is one or a mixture of SAPO-17, SAPO-18, SAPO-34, SAPO-44, SAPO-35, and SAPO-56.
- the alkali metal-containing source is one or a mixture of oxides, inorganic salts or organic salts of calcium, barium or strontium; the source of the transition metal is copper or zinc.
- the modified molecular sieve prepared by the high-temperature calcination removal of the template has a mass content of 0.1-5 %.
- the modified molecular sieve prepared by the high-temperature calcination removal of the templating agent has a metal content of 0.5-3%.
- the preparation method is as follows: a) hydrothermal synthesis of small pores SAPO molecular sieve, drying at 100-120 ° C, to obtain molecular sieve raw powder;
- modified small pore SAPO molecular sieve obtained in the step b) is dried at 120 ° C, and calcined in air at 500-700 ° C for 3-8 hours to obtain a modified SAPO molecular sieve catalyst.
- the modified molecular sieve catalyst obtained by the method of the invention can be applied to the conversion of oxygenates to olefins, and the modified molecular sieves exhibit higher initial selectivity of lower olefins than unmodified molecular sieves.
- the method of the invention adopts a method of impregnation or mechanical grinding to mix a compound containing an alkali metal (calcium, barium or strontium) and/or a transition metal (copper or zinc) with a small-porous phosphosilica molecular sieve raw powder (such as SAPO-34). Mixing, preparing modified molecular sieves.
- a compound containing an alkali metal calcium, barium or strontium
- a transition metal copper or zinc
- the invention is characterized in that the small pore silicon aluminum molecular sieve used is one or a mixture of any one of SAPO-17, SAPO-18, SAPO-34, SAPO-44, SAPO-35, SAPO-56.
- step b) The modified pores obtained in step b) are dried at 120 ° C and calcined in air at 500-700 ° C.
- the modified SAPO molecular sieve catalyst was obtained in 3-8 hours.
- the present invention is characterized in that the source of the metal used is one or a mixture of oxides, inorganic salts or organic salts of calcium, barium, strontium, copper or zinc. After the modified molecular sieve is calcined at a high temperature to remove the templating agent, the metal content thereof is 0.1-5%.
- the invention is described in detail below by way of examples.
- the modified SAPO-34 molecular sieve catalyst obtained in Example 1-4 was used for methanol to olefin catalytic reaction, and the unmodified SAPO-34 molecular sieve raw powder was calcined and the template was also calcined to evaluate the reaction.
- Reaction conditions 2.5 g of a sample of 20-40 mesh granule catalyst was charged into a reactor, activated by nitrogen at 550 ° C for 1 hour, and then cooled to 50 (TC was carried out. The nitrogen was used as a diluent gas to carry the raw material methanol, nitrogen flow rate The molecular weight of the methanol was 2.01 ⁇ at 40 ml/min.
- the composition of the reaction product was analyzed by on-line gas chromatography, and the results are shown in Table 1.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Procédé de modification d'un tamis moléculaire à micropores de silicoaluminium phosphate au moyen d'un métal. Ce procédé consiste à mélanger une poudre de tamis moléculaires de silicoaluminium phosphate, tel que SAPO-34, avec un composé alcalino-terreux (CA, Sr ou Ba) et/ou un métal de transition (Cu iz Zn) par un procédé d'immersion ou par broyage. Ainsi modifié, le tamis moléculaire peut s'utiliser comme catalyseur pour transformer des charges de produits oxygénées en oléfines et présente pour les oléfines à faible teneur en carbone une séléctivité initiale plus élevée que des tamis moléculaires non modifiés.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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CN200610089170 | 2006-08-08 | ||
CN200610089170.7 | 2006-08-08 | ||
CN200610160685.1 | 2006-12-04 | ||
CNA2006101606851A CN101121532A (zh) | 2006-08-08 | 2006-12-04 | 一种小孔磷硅铝分子筛的金属改性方法 |
Publications (1)
Publication Number | Publication Date |
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WO2008019585A1 true WO2008019585A1 (fr) | 2008-02-21 |
Family
ID=39081929
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/CN2007/002349 WO2008019585A1 (fr) | 2006-08-08 | 2007-08-06 | Procédé de modification d'un tamis moléculaire à micropores de silicoaluminium phosphate au moyen d'un métal |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN101121532A (fr) |
WO (1) | WO2008019585A1 (fr) |
Cited By (12)
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US7601662B2 (en) | 2007-02-27 | 2009-10-13 | Basf Catalysts Llc | Copper CHA zeolite catalysts |
US7998423B2 (en) | 2007-02-27 | 2011-08-16 | Basf Corporation | SCR on low thermal mass filter substrates |
US8293199B2 (en) | 2009-12-18 | 2012-10-23 | Basf Corporation | Process for preparation of copper containing molecular sieves with the CHA structure, catalysts, systems and methods |
US8293198B2 (en) | 2009-12-18 | 2012-10-23 | Basf Corporation | Process of direct copper exchange into Na+-form of chabazite molecular sieve, and catalysts, systems and methods |
US8603432B2 (en) | 2007-04-26 | 2013-12-10 | Paul Joseph Andersen | Transition metal/zeolite SCR catalysts |
US8617474B2 (en) | 2008-01-31 | 2013-12-31 | Basf Corporation | Systems utilizing non-zeolitic metal-containing molecular sieves having the CHA crystal structure |
CN108262068A (zh) * | 2017-01-04 | 2018-07-10 | 中国石油化工股份有限公司 | 含氧物制低碳烯烃的方法 |
US10583424B2 (en) | 2008-11-06 | 2020-03-10 | Basf Corporation | Chabazite zeolite catalysts having low silica to alumina ratios |
CN112250087A (zh) * | 2020-11-08 | 2021-01-22 | 江西苏克尔新材料有限公司 | 一种金属改性的sapo-34分子筛的制备方法及应用 |
CN115672393A (zh) * | 2021-07-28 | 2023-02-03 | 国家能源投资集团有限责任公司 | 甲醇转化制低碳烯烃用催化剂及其制备方法、甲醇转化制备低碳烯烃的方法 |
CN116493041A (zh) * | 2023-05-30 | 2023-07-28 | 天津大沽化工股份有限公司 | 一种用于1,2-二氯乙烷制氯乙烯的复合催化剂及其制备方法 |
CN115672393B (zh) * | 2021-07-28 | 2024-06-04 | 国家能源投资集团有限责任公司 | 甲醇转化制低碳烯烃用催化剂及其制备方法、甲醇转化制备低碳烯烃的方法 |
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CN101519391B (zh) * | 2008-02-28 | 2011-07-20 | 中国科学院大连化学物理研究所 | 一种制备环氧丙烷的方法 |
CN101632939B (zh) * | 2008-07-24 | 2015-07-29 | 中国石油化工股份有限公司 | 一种含磷酸硅铝分子筛的组合物、制备方法及其应用 |
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