CN107971020A - A kind of preparation method of MTO catalyst carrier - Google Patents
A kind of preparation method of MTO catalyst carrier Download PDFInfo
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- CN107971020A CN107971020A CN201711275072.7A CN201711275072A CN107971020A CN 107971020 A CN107971020 A CN 107971020A CN 201711275072 A CN201711275072 A CN 201711275072A CN 107971020 A CN107971020 A CN 107971020A
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- 239000003054 catalyst Substances 0.000 title claims abstract description 14
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- 239000002131 composite material Substances 0.000 claims abstract description 33
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000003756 stirring Methods 0.000 claims abstract description 24
- 230000004048 modification Effects 0.000 claims abstract description 22
- 238000012986 modification Methods 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 16
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 15
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 15
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000010457 zeolite Substances 0.000 claims abstract description 15
- 239000008187 granular material Substances 0.000 claims abstract description 12
- 239000000843 powder Substances 0.000 claims abstract description 12
- 238000006243 chemical reaction Methods 0.000 claims abstract description 10
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000011574 phosphorus Substances 0.000 claims abstract description 9
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 9
- 238000002425 crystallisation Methods 0.000 claims abstract description 8
- 230000008025 crystallization Effects 0.000 claims abstract description 8
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims abstract description 7
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 7
- 239000010703 silicon Substances 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims abstract 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 26
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 20
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 claims description 20
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 16
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 16
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 15
- 239000000377 silicon dioxide Substances 0.000 claims description 13
- 229910001923 silver oxide Inorganic materials 0.000 claims description 10
- 239000004408 titanium dioxide Substances 0.000 claims description 10
- 239000002253 acid Substances 0.000 claims description 9
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical group C1COCCN1 YNAVUWVOSKDBBP-UHFFFAOYSA-N 0.000 claims description 8
- 235000011007 phosphoric acid Nutrition 0.000 claims description 8
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 6
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 6
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 claims description 6
- 229910001593 boehmite Inorganic materials 0.000 claims description 6
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical group O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 claims description 6
- 150000003053 piperidines Chemical class 0.000 claims description 6
- -1 polyethylene Polymers 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 239000004698 Polyethylene Substances 0.000 claims description 5
- 239000011812 mixed powder Substances 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 229920000573 polyethylene Polymers 0.000 claims description 5
- 238000005406 washing Methods 0.000 claims description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 4
- 239000004411 aluminium Substances 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims description 2
- 235000019253 formic acid Nutrition 0.000 claims description 2
- 229910017604 nitric acid Inorganic materials 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 239000002808 molecular sieve Substances 0.000 abstract description 5
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 abstract description 5
- 230000003197 catalytic effect Effects 0.000 abstract description 3
- 238000011031 large-scale manufacturing process Methods 0.000 abstract description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 abstract 3
- 238000004064 recycling Methods 0.000 abstract 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 239000008367 deionised water Substances 0.000 description 6
- 229910021641 deionized water Inorganic materials 0.000 description 6
- 150000001336 alkenes Chemical class 0.000 description 5
- 239000011259 mixed solution Substances 0.000 description 4
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 3
- 229910021502 aluminium hydroxide Inorganic materials 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical class O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 239000002114 nanocomposite Substances 0.000 description 1
- 239000011858 nanopowder Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002195 synergetic effect Effects 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
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/80—Mixtures of different zeolites
-
- 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
- B01J29/005—Mixtures of molecular sieves comprising at least one molecular sieve which is not an aluminosilicate zeolite, e.g. from groups B01J29/03 - B01J29/049 or B01J29/82 - B01J29/89
-
- 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
-
- 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
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
- B01J29/42—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively containing iron group metals, noble metals or copper
- B01J29/44—Noble 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/82—Phosphates
- B01J29/83—Aluminophosphates [APO 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
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2529/00—Catalysts comprising molecular sieves
- C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
- C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- C07C2529/80—Mixtures of different zeolites
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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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- 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
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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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
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
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- Chemical & Material Sciences (AREA)
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- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The object of the present invention is to provide a kind of preparation method of MTO catalyst carrier.Comprise the following steps that：Prepare nano modification composite granule, take silicon source, phosphorus source, water, 5 original powders of ZSM and nano modification composite granule, template is sequentially added after stirring and evenly mixing, Zeolite synthesis gel is made in hydrofluoric acid, by Zeolite synthesis gel after Crystallizing treatment, recycling crystallization product is up to 34 composite molecular screens of ZSM 5/AlPO4.MTO catalyst carrier is used as using the molecular sieve.The method that the present invention prepares 34 composite molecular screens of ZSM 5/AlPO4 is simple, and crystallization time is shorter, suitable for large-scale production and application, its remarkable in economical benefits.It is applied to the selectivity and catalytic efficiency that reaction can be significantly improved in MTO reactions using 34 composite molecular screens of ZSM 5/AlPO4 made from the method for the present invention.
Description
Technical field
The present invention relates to a kind of method for preparing MTO catalyst carrier, belong to technical field of chemical synthesis.
Background technology
MTO (Methanol To Olefin) refers to by preparing low carbon olefinic hydrocarbon with methanol（Ethene and propylene）Chemical process skill
Art, a new raw material route has been found for alkene production.Without oil using methanol as olefin production, it can not only make alkene
Hydrocarbon price breaks away from the influence of oil product, moreover it is possible to reduces China and petroleum resources are depended on unduly.
The key of MTO technologies is the development of high performance catalyst, and the research for MTO catalyst is mainly with ZSM-5 in early days
Based on mesoporous molecular sieve, the advantages that middle macroporous structure of ZSM-5 makes it have few low-carbon, long lifespan, but since it is acid
It is too strong, while have the shortcomings that the low accessory substance of olefin yields is more again.1984, UCC companies invented SAPO-34 molecular sieves and have been used for
MTO reacts, its less aperture and larger specific surface area accelerate MTO reaction rates and improve the selectivity of reaction,
But there is high carbon distribution, easy in inactivation and short life.
In view of the application in methanol to olefins reaction is, it is necessary to prepare a kind of ZSM-5/ aluminum phosphates composite molecular screen, with ZSM-5
Compare, ZSM-5/ aluminum phosphate composite molecular screens show good synergistic effect and excellent catalytic performance.
The content of the invention
In order to solve the above-mentioned technical problem, the object of the present invention is to provide a kind of method for preparing MTO catalyst carrier, tool
Body step is as follows：
（1）The mixed powder for taking particle diameter to be the silica of 40-50nm, titanium dioxide and silver oxide is added in container, wherein
The mass ratio of silica, titanium dioxide and silver oxide is 2.8：2：1.6, the mixed solution of polyethylene alcohol and water is then added,
It is dispersed with stirring at room temperature 60 minutes, then adds Silane coupling agent KH550 and acid, wherein KH550 is 1 with sour molar ratio:1,
70 DEG C of stirring reaction 5h, are then cooled to room temperature, filter, obtain nano modification composite granule；
（2）By silicon source, phosphorus source be added to the water stirring it is to be dissolved completely, add ZSM-5 original powders and step（1）Obtained nanometer changes
Property composite granule continue to stir, and add template, hydrofluoric acid, it is to be mixed 3~5 it is small when after nano modification Zeolite synthesis is made
Gel；
（3）By step（2）Zeolite synthesis gel when crystallization 12~24 is small at 150~190 DEG C postcooling to room temperature, mistake
Filter, it is washing, dry at 60-80 DEG C, then up to nano modification composite molecular screen when roasting 4~8 is small at 350~580 DEG C；
（4）By step（3）In obtained nano modification composite molecular screen be used for MTO catalyst as carrier.
Source of aluminium, phosphorus source, template, the molar ratio of hydrofluoric acid and water are silicon source:Phosphorus source:Template:Hydrofluoric acid：Water=
1:（1.0~1.5）:（0.5~2）:（0.1~0.2）：（50~300）；
The template is morpholine, piperidines or pyridine.
The silicon source is one or both of boehmite, aluminium isopropoxide, aluminium hydroxide, aluminium oxide arbitrary proportion
Mixture.
The phosphorus source is orthophosphoric acid.
Step（1）In one or more of the acid in hydrochloric acid, nitric acid, formic acid, acetic acid.
Step（3）For middle synthesized gel rubber when 160~180 DEG C of hydrothermal crystallizings 18 are small, drying temperature is 60~80 DEG C.
The quality of the ZSM-5 original powders accounts for about the 1/10~1/5 of Zeolite synthesis gel total amount.
Beneficial effects of the present invention：
The method that the present invention prepares nano modification ZSM-5/AlPO4-34 composite molecular screens is simple, and crystallization time is shorter, suitable for big
Large-scale production application, its remarkable in economical benefits.The modified Nano composite granule of specific proportioning is additionally used in molecular sieve, by table
The above-mentioned composite nano-powder that face is modified can be effectively improved adhesion, intensity, toughness and the heat-resisting quantity of molecular sieve.ZSM-5/
The mutual collaboration of each component, can significantly improve anti-in being reacted applied to MTO in AlPO4-34 composite molecular screen specific compositions
The selectivity and catalytic efficiency answered.
Embodiment
Embodiment 1
The preparation method of nano modification ZSM-5/AlPO4-34 composite molecular screens specifically includes following steps in the present embodiment：
（1）The mixed powder for taking particle diameter to be the silica of 40-50nm, titanium dioxide and silver oxide is added in container, wherein
The mass ratio of silica, titanium dioxide and silver oxide is 2.8：2：1.6, the mixed solution of polyethylene alcohol and water is then added,
It is dispersed with stirring at room temperature 60 minutes, then adds Silane coupling agent KH550 and acid, wherein KH550 is 1 with sour molar ratio:1,
70 DEG C of stirring reaction 5h, are then cooled to room temperature, filter, obtain nano modification composite granule；
（2）It is according to molar ratio（Aluminium isopropoxide+aluminium oxide）:Orthophosphoric acid:（Piperidines+pyridine）:Hydrofluoric acid：Deionized water=1:
1.0:0.5:0.1：50 take each component, by aluminium isopropoxide and aluminium oxide stone be added into respectively in deionized water stirring 6 it is small when, treat
When addition orthophosphoric acid stirring 3 is small after dissolving completely, ZSM-5 original powders and step that silica alumina ratio is 50 are added（1）Obtained nanometer
Modified composite powder body continues to stir, and adds piperidines and pyridine, and hydrofluoric acid, and the quality of ZSM-5 original powders accounts for Zeolite synthesis
The 1/5 of gel total amount, it is to be mixed 3 it is small when Zeolite synthesis gel is made；
（3）By step（2）Middle Zeolite synthesis gel is moved in the stainless steel crystallizing kettle with polytetrafluoroethyllining lining, at 150 DEG C
Postcooling is filtered to room temperature when lower crystallization 24 is small, after washing to neutrality at 80 DEG C it is dry 6 it is small when, then roast 4 at 580 DEG C
Hour is up to ZSM-5/AlPO4-34 composite molecular screens；
（4）By step（3）In obtained nano modification composite molecular screen be used for MTO catalyst as carrier.
Embodiment 2
The preparation method of nano modification ZSM-5/AlPO4-34 composite molecular screens specifically includes following steps in the present embodiment：
（1）The mixed powder for taking particle diameter to be the silica of 40-50nm, titanium dioxide and silver oxide is added in container, wherein
The mass ratio of silica, titanium dioxide and silver oxide is 2.8：2：1.6, the mixed solution of polyethylene alcohol and water is then added,
It is dispersed with stirring at room temperature 60 minutes, then adds Silane coupling agent KH550 and acid, wherein KH550 is 1 with sour molar ratio:1,
70 DEG C of stirring reaction 5h, are then cooled to room temperature, filter, obtain nano modification composite granule；
（2）It is according to molar ratio（Aluminium hydroxide+boehmite）:Orthophosphoric acid:（Morpholine+pyridine）:Hydrofluoric acid：Deionized water=
1: 1.2: 1: 0.15：200 take each component, and aluminium hydroxide and boehmite are added into deionized water respectively and stir 8
Hour, it is to be dissolved completely after add orthophosphoric acid stirring 3 it is small when, add silica alumina ratio be 50 ZSM-5 original powders and step（1）Obtain
Nano modification composite granule continue to stir, and add morpholine and pyridine, and hydrofluoric acid, the quality of ZSM-5 original powders account for molecule
Sieve synthesized gel rubber total amount 1/7, it is to be mixed 4 it is small when Zeolite synthesis gel is made；
（3）By step（2）Middle Zeolite synthesis gel is moved in the stainless steel crystallizing kettle with polytetrafluoroethyllining lining, 180
When crystallization 18 is small at DEG C, room temperature is subsequently cooled to, is filtered, when drying 8 is small at 70 DEG C after washing to neutrality, then at 450 DEG C
Roast 6 it is small when up to ZSM-5/AlPO4-34 composite molecular screens；
（4）By step（3）In obtained nano modification composite molecular screen be used for MTO catalyst as carrier.
Embodiment 3
The preparation method of nano modification ZSM-5/AlPO4-34 composite molecular screens specifically includes following steps in the present embodiment：
（1）The mixed powder for taking particle diameter to be the silica of 40-50nm, titanium dioxide and silver oxide is added in container, wherein
The mass ratio of silica, titanium dioxide and silver oxide is 2.8：2：1.6, the mixed solution of polyethylene alcohol and water is then added,
It is dispersed with stirring at room temperature 60 minutes, then adds Silane coupling agent KH550 and acid, wherein KH550 is 1 with sour molar ratio:1,
70 DEG C of stirring reaction 5h, are then cooled to room temperature, filter, obtain nano modification composite granule；
（2）It is according to molar ratio（Aluminium isopropoxide+boehmite）:Orthophosphoric acid:（Piperidines+pyridine）:Hydrofluoric acid：Deionized water=
1: 1.5: 2: 0.2：300 take each component, and aluminium isopropoxide and boehmite are added into deionized water respectively and stir 8
Hour, it is to be dissolved completely after add orthophosphoric acid stirring 3 it is small when, add silica alumina ratio be 50 ZSM-5 original powders and step（1）Obtain
Nano modification composite granule continue to stir, and add piperidines and pyridine, and hydrofluoric acid, the quality of ZSM-5 original powders account for molecule
Sieve synthesized gel rubber total amount 1/5, it is to be mixed 5 it is small when Zeolite synthesis gel is made；
（3）By step（2）Middle Zeolite synthesis gel is moved in the stainless steel crystallizing kettle with polytetrafluoroethyllining lining, 190
When crystallization 12 is small at DEG C, room temperature is subsequently cooled to, is filtered, when drying 10 is small at 60 DEG C after washing to neutrality, then at 350 DEG C
Roast 8 it is small when up to ZSM-5/AlPO4-34 composite molecular screens；
（4）By step（3）In obtained nano modification composite molecular screen be used for MTO catalyst as carrier.
Claims (3)
- A kind of 1. preparation method of MTO catalyst carrier, it is characterised in that：Comprise the following steps that：（1）The mixed powder that particle diameter is each about the silica of 40-50nm, titanium dioxide and silver oxide is taken to add in container, its The mass ratio of middle silica, titanium dioxide and silver oxide is 2.8：2：1.6, the mixing for then adding polyethylene alcohol and water is molten Liquid, is dispersed with stirring 60 minutes at room temperature, then adds Silane coupling agent KH550 and acid, wherein Silane coupling agent KH550 and acid Molar ratio is 1:1,70 DEG C of stirring reaction 5h, is then cooled to room temperature, filters, obtain nano modification composite granule；（2）By silicon source, phosphorus source be added to the water stirring it is to be dissolved completely, add ZSM-5 original powders and step（1）Obtained nanometer changes Property composite granule continue to stir, and add template, hydrofluoric acid, it is to be mixed 3~5 it is small when after nano modification Zeolite synthesis is made Gel；（3）By step（2）Zeolite synthesis gel postcooling is to room temperature when crystallization 18 is small at about 160~180 DEG C, filtering, It is washing, dry at 70 DEG C, then up to nano modification composite molecular screen when roasting 4~8 is small at 350~580 DEG C；（4）By step（3）In obtained nano modification composite molecular screen be used for MTO catalyst as carrier；Source of aluminium, phosphorus source, template, the molar ratio of hydrofluoric acid and water are silicon source:Phosphorus source:Template:Hydrofluoric acid：Water=1: （1.0~1.5）:（0.5~2）:（0.1~0.2）：（50~300）；The template is morpholine, piperidines or pyridine；The phosphorus source is orthophosphoric acid；Step（1）In one or more of the acid in hydrochloric acid, nitric acid, formic acid, acetic acid.
- 2. according to the method described in claim 1, it is characterized in that：The quality of the ZSM-5 original powders accounts for Zeolite synthesis gel The 1/10~1/5 of total amount.
- 3. according to the method described in claim 1, it is characterized in that：The silicon source is boehmite, aluminium isopropoxide, hydrogen-oxygen Change the mixture of one or both of aluminium, aluminium oxide arbitrary proportion.
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