WO2008019580A1 - Tamis moléculaire à micropores modifié par phosphore de silicoaluminium phosphate, son procédé de fabrication et son utilisation - Google Patents
Tamis moléculaire à micropores modifié par phosphore de silicoaluminium phosphate, son procédé de fabrication et son utilisation Download PDFInfo
- Publication number
- WO2008019580A1 WO2008019580A1 PCT/CN2007/002310 CN2007002310W WO2008019580A1 WO 2008019580 A1 WO2008019580 A1 WO 2008019580A1 CN 2007002310 W CN2007002310 W CN 2007002310W WO 2008019580 A1 WO2008019580 A1 WO 2008019580A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- molecular sieve
- phosphorus
- sapo
- modified
- phosphosilica
- Prior art date
Links
- 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 54
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 45
- 238000000034 method Methods 0.000 title claims abstract description 20
- 229910019142 PO4 Inorganic materials 0.000 title claims abstract description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 title claims abstract description 5
- 239000010452 phosphate Substances 0.000 title claims abstract description 5
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 22
- 239000011574 phosphorus Substances 0.000 claims abstract description 22
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 21
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000000843 powder Substances 0.000 claims abstract description 13
- 150000001336 alkenes Chemical class 0.000 claims abstract description 11
- 150000001875 compounds Chemical class 0.000 claims abstract description 10
- 229910000073 phosphorus hydride Inorganic materials 0.000 claims abstract description 7
- 238000007654 immersion Methods 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 17
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 239000011148 porous material Substances 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 12
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical group CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 238000002715 modification method Methods 0.000 claims description 4
- 235000011007 phosphoric acid Nutrition 0.000 claims description 4
- 238000007598 dipping method Methods 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 claims description 3
- 238000001354 calcination Methods 0.000 claims description 2
- AUONHKJOIZSQGR-UHFFFAOYSA-N oxophosphane Chemical compound P=O AUONHKJOIZSQGR-UHFFFAOYSA-N 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 abstract description 18
- 229910052799 carbon Inorganic materials 0.000 abstract description 7
- -1 SAPO-34 Chemical compound 0.000 abstract description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 27
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 7
- 229910021536 Zeolite Inorganic materials 0.000 description 6
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000010457 zeolite Substances 0.000 description 6
- 241000269350 Anura Species 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- URLKBWYHVLBVBO-UHFFFAOYSA-N Para-Xylene Chemical group CC1=CC=C(C)C=C1 URLKBWYHVLBVBO-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 2
- 229910052761 rare earth metal Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 1
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 description 1
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 239000013522 chelant Substances 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
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000007323 disproportionation reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 125000001145 hydrido group Chemical group *[H] 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000007069 methylation reaction Methods 0.000 description 1
- 235000019837 monoammonium phosphate Nutrition 0.000 description 1
- VMGAPWLDMVPYIA-HIDZBRGKSA-N n'-amino-n-iminomethanimidamide Chemical compound N\N=C\N=N VMGAPWLDMVPYIA-HIDZBRGKSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000003348 petrochemical agent Substances 0.000 description 1
- UEZVMMHDMIWARA-UHFFFAOYSA-M phosphonate Chemical compound [O-]P(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-M 0.000 description 1
- 150000003017 phosphorus Chemical class 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- BOLDJAUMGUJJKM-LSDHHAIUSA-N renifolin D Natural products CC(=C)[C@@H]1Cc2c(O)c(O)ccc2[C@H]1CC(=O)c3ccc(O)cc3O BOLDJAUMGUJJKM-LSDHHAIUSA-N 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000006177 thiolation reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C01B37/00—Compounds having molecular sieve properties but not having base-exchange properties
- C01B37/06—Aluminophosphates containing other elements, e.g. metals, boron
- C01B37/08—Silicoaluminophosphates [SAPO compounds], e.g. CoSAPO
-
- 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
- B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
- B01J2229/186—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions
Definitions
- the invention relates to a phosphorus modification method for a small pore phosphosilica molecular sieve, and a catalytic application of the molecular sieve catalyst prepared by the method for the conversion of an oxygenate to a low carbon olefin.
- 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 . With the advent of silicoaluminophosphate series molecular sieves, 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). It is about 0.43 nm and is a good type of shape-selective catalyst.
- SAPO-34 molecular sieve has become a hot spot in current research because of its excellent acidity and pore structure and excellent catalytic performance in MTO reaction.
- Using SAPO-34 molecular sieve as catalyst in 1995 UOP Company of Norway and Norsk Hydro Company of Norway completed the MTO fluidized bed pilot test for 0.5 t / d methanol.
- the Dalian Institute of Chemical Physics of the Chinese Academy of Sciences completed the synthesis gas. Pilot test for the preparation of light olefins via dimethyl ether.
- CN102247 reports the preparation of zeolite-catalyst (ZSM-5) modified with phosphorus-rare earth and its application in the process of toluene disproportionation and toluene and ethylene thiolation.
- ZSM-5 zeolite catalyst modified with phosphorus and used for the alkylation of methyl styrene to obtain p-toluene, so that the isomer of p-toluene is up to 96% or more.
- CN1176752 reports a method for catalyzing the catalytic activity of zeolite molecular sieves for catalytic cracking reaction, that is, adding phosphorus and rare earth compounds to zeolite molecular sieves, reacting at room temperature for a period of time, filtering and drying to obtain modified products.
- CN1704167 provides a catalyst for zeolite Row modification to increase the selectivity to para-xylene in the methylation reaction of toluene.
- the method comprises: forming a slurry of an aqueous solution of ZSM-5 zeolite and a phosphorus compound; removing water from the slurry to provide a non-steam treated, phosphorus-treated ZSM-5 zeolite catalyst without passing through an organic phosphorus vapor Deposited on the catalyst.
- W09928277 reports an oxygen-containing chelate reagent for treating small pore molecular sieves.
- the modified molecular sieve is used as a catalyst for the conversion of oxygenates to olefins, which can effectively reduce the selectivity of formazan.
- the object of the present invention is to provide a phosphorus modification method for a small pore phosphosilica molecular sieve, which comprises mixing an inorganic phosphorus or an organic phosphine-containing compound with a small-porous phosphosilica molecular sieve raw powder by a dipping method to prepare a modified molecular sieve.
- the present invention is characterized in that the small pore phosphosilicate aluminum molecular sieve used is one or a mixture of SAPO-17, SAPO-18, SAPO-34, SAPO-44, SAPO-35, SAPO-56.
- the phosphorus modification method of the present invention is prepared as follows:
- the compound containing the organic phosphine is dissolved in an organic solvent (such as ethanol or toluene, etc.), and the molecular sieve raw powder is impregnated at room temperature for 1-24 hours ;
- the modified small pore SAPO molecular sieve obtained in the step b) is dried at 80 to 120 ° C, and calcined in air at 500-700 ° C for 3 to 8 hours to obtain a modified SAPO molecular sieve catalyst.
- the inorganic phosphorus-containing compound of the present invention is one or a mixture of orthophosphoric acid and soluble phosphate.
- the organic phosphine-containing compound of the present invention is a mixture of one or more of an organic phosphine or a phosphine oxide.
- the phosphorus-modified small-porosity silicalite molecular sieve of the present invention has a mass content of phosphorus of 0.1 to 5% increased in the sample obtained by calcination.
- the modified molecular sieve catalyst obtained by the invention can be applied to the conversion of an oxygenate to an olefin, and the modified molecular sieve has an initial selectivity to the lower olefin of the unmodified molecular sieve.
- the modified SAPO-34 molecular sieve catalyst obtained in Example 1-3 was used for methanol to olefin catalytic reaction, and the unmodified SAPO-34 molecular sieve raw powder was calcined in air for 600 hours, and the organic template was completely removed.
- Nitrogen was used as a diluent gas to carry the raw material methanol, the nitrogen flow rate was 40 ml/min, and the methanol weight space velocity lOl ⁇ reaction product composition was analyzed by on-line gas chromatography. The results are shown in Table 1.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Tamis moléculaire à micropores modifié par phosphore de silicoaluminium phosphate, son procédé de fabrication et son utilisation. Ce procédé consiste à mélanger la poudre du tamis moléculaire de silicoaluminium phosphate, tel que SAPO-34, avec un composé de phosphore inorganique ou phosphine selon un procédé d'immersion. Le tamis moléculaire modifié, qui peut s'utiliser comme catalyseur pour transformer une charge de composé oxygéné en oléfines, présente pour les oléfines à faible teneur en carbone une sélectivité supérieure à celle de tamis moléculaires non modifiés.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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CN200610089169 | 2006-08-08 | ||
CN200610089169.4 | 2006-08-08 | ||
CN200610160684.7 | 2006-12-04 | ||
CNA2006101606847A CN101121531A (zh) | 2006-08-08 | 2006-12-04 | 一种小孔磷硅铝分子筛的磷改性方法 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2008019580A1 true WO2008019580A1 (fr) | 2008-02-21 |
Family
ID=39081926
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2007/002310 WO2008019580A1 (fr) | 2006-08-08 | 2007-07-31 | Tamis moléculaire à micropores modifié par phosphore de silicoaluminium phosphate, son procédé de fabrication et son utilisation |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN101121531A (fr) |
WO (1) | WO2008019580A1 (fr) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102992349A (zh) * | 2012-12-11 | 2013-03-27 | 陕西煤化工技术工程中心有限公司 | 一种sapo-34分子筛合成母液的循环利用方法 |
CN113526522A (zh) * | 2020-04-13 | 2021-10-22 | 中国石油化工股份有限公司 | 磷改性mfi结构分子筛及其制备方法 |
CN114713277A (zh) * | 2021-01-05 | 2022-07-08 | 中国石油化工股份有限公司 | 一种改性mfi结构硅铝分子筛及其制备方法 |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
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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 |
CN101633509B (zh) * | 2008-07-24 | 2012-02-29 | 中国石油化工股份有限公司 | 一种磷酸硅铝分子筛的改性方法 |
CN103566967B (zh) * | 2012-08-03 | 2016-01-20 | 中国石油化工股份有限公司 | 一种烯烃异构化催化剂及其制备方法 |
CN103769208B (zh) * | 2012-10-24 | 2016-08-03 | 中国石油化工股份有限公司 | 一种磷改性的sapo-11分子筛催化剂及其制备方法和应用 |
CN106064823A (zh) * | 2016-05-30 | 2016-11-02 | 中国天辰工程有限公司 | 一种改性sapo‑34分子筛的方法 |
CN109647503B (zh) * | 2017-10-10 | 2021-11-16 | 中国石油化工股份有限公司 | 一种由合成气制备低碳烯烃的复合催化剂及其制备方法和由合成气制备低碳烯烃的方法 |
CN110801862A (zh) * | 2019-10-24 | 2020-02-18 | 杜成荣 | 一种甲醇制备低碳烯烃的催化剂 |
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US4605637A (en) * | 1983-02-14 | 1986-08-12 | Mobil Oil Corporation | Hydrothermal activation of acid zeolites with aluminum phosphates |
US5378670A (en) * | 1993-04-16 | 1995-01-03 | W. R. Grace & Co.-Conn. | Phosphorus zeolites/molecular sieves |
CN1291915A (zh) * | 1998-03-11 | 2001-04-18 | 埃克森化学专利公司 | 用磷酸铝和磷提高沸石催化剂的活性 |
US20060106270A1 (en) * | 2004-11-12 | 2006-05-18 | Glover Bryan K | Selective conversion of oxygenate to propylene using moving bed technology and a hydrothermally stabilized dual-function catalyst |
-
2006
- 2006-12-04 CN CNA2006101606847A patent/CN101121531A/zh active Pending
-
2007
- 2007-07-31 WO PCT/CN2007/002310 patent/WO2008019580A1/fr active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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US4605637A (en) * | 1983-02-14 | 1986-08-12 | Mobil Oil Corporation | Hydrothermal activation of acid zeolites with aluminum phosphates |
US5378670A (en) * | 1993-04-16 | 1995-01-03 | W. R. Grace & Co.-Conn. | Phosphorus zeolites/molecular sieves |
CN1291915A (zh) * | 1998-03-11 | 2001-04-18 | 埃克森化学专利公司 | 用磷酸铝和磷提高沸石催化剂的活性 |
US20060106270A1 (en) * | 2004-11-12 | 2006-05-18 | Glover Bryan K | Selective conversion of oxygenate to propylene using moving bed technology and a hydrothermally stabilized dual-function catalyst |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102992349A (zh) * | 2012-12-11 | 2013-03-27 | 陕西煤化工技术工程中心有限公司 | 一种sapo-34分子筛合成母液的循环利用方法 |
CN113526522A (zh) * | 2020-04-13 | 2021-10-22 | 中国石油化工股份有限公司 | 磷改性mfi结构分子筛及其制备方法 |
CN113526522B (zh) * | 2020-04-13 | 2023-02-21 | 中国石油化工股份有限公司 | 磷改性mfi结构分子筛及其制备方法 |
CN114713277A (zh) * | 2021-01-05 | 2022-07-08 | 中国石油化工股份有限公司 | 一种改性mfi结构硅铝分子筛及其制备方法 |
CN114713277B (zh) * | 2021-01-05 | 2023-07-14 | 中国石油化工股份有限公司 | 一种改性mfi结构硅铝分子筛及其制备方法 |
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