CN109205636A - The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material - Google Patents

The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material Download PDF

Info

Publication number
CN109205636A
CN109205636A CN201710519563.5A CN201710519563A CN109205636A CN 109205636 A CN109205636 A CN 109205636A CN 201710519563 A CN201710519563 A CN 201710519563A CN 109205636 A CN109205636 A CN 109205636A
Authority
CN
China
Prior art keywords
zsm
sapo
molecular sieve
solution
asa
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201710519563.5A
Other languages
Chinese (zh)
Other versions
CN109205636B (en
Inventor
李海岩
孙发民
谢方明
姜维
张全国
丛丽茹
赵檀
关旭
董春明
王亮
于春梅
秦丽红
马守涛
吴显军
张文成
郭金涛
王刚
焦庆雨
孙宏磊
李军
吕倩
王甫村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Petroleum and Natural Gas Co Ltd
Original Assignee
China Petroleum and Natural Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China Petroleum and Natural Gas Co Ltd filed Critical China Petroleum and Natural Gas Co Ltd
Priority to CN201710519563.5A priority Critical patent/CN109205636B/en
Publication of CN109205636A publication Critical patent/CN109205636A/en
Application granted granted Critical
Publication of CN109205636B publication Critical patent/CN109205636B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B37/00Compounds having molecular sieve properties but not having base-exchange properties
    • C01B37/06Aluminophosphates containing other elements, e.g. metals, boron
    • C01B37/08Silicoaluminophosphates (SAPO compounds), e.g. CoSAPO
    • B01J35/633
    • B01J35/635
    • B01J35/643
    • B01J35/647
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
    • C01B39/36Pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • C01B39/365Type ZSM-8; Type ZSM-11; ZSM 5/11 intermediate
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/54Phosphates, e.g. APO or SAPO compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12Inorganic carriers
    • C10G47/16Crystalline alumino-silicate carriers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/20After 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

Abstract

The present invention provides a kind of Y/SAPO-34/ZSM-11/ASA multilevel hole material preparation methods, it is characterized in that this method comprises: first synthesizing directed agents, Y/SAPO-34/ZSM-11 composite molecular screen is synthesized using hydrothermal crystallization method, then surfactant, alkaline silicon source and/or alkaline silicon source solution are added in the slurries of Y/SAPO-34/ZSM-11 molecular sieve, product is washed, dry, roasting is to get mesoporous Y/SAPO-34/ZSM-11/ASA multilevel hole material.

Description

The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material
Technical field
The present invention provides a kind of Y/SAPO-34/ZSM-11/ASA multilevel hole material preparation method, first synthesis directed agents, Y/SAPO-34/ZSM-11 composite molecular screen is synthesized using hydrothermal crystallization method, then in the slurry of Y/SAPO-34/ZSM-11 molecular sieve Be added surfactant, alkaline silicon source and/or alkaline silicon source solution in liquid, product is washed, it is dry, roast to get mesoporous Y/ SAPO-34/ZSM-11/ASA composite material.
Background technique
Molecular sieve complex, which refers to, is incorporated in one by molecule, atom or interionic effect by molecular sieve and other materials The composite material risen.Regular material with meso-hole structure such as MCM-41 mesopore molecular sieve is suitble to because of its biggish cellular structure In the conversion of organic macromolecule, but its poor thermal stability, hydrothermal stability and weaker acidity limit this kind of materials In the application of catalytic field.The research of micropore-mesopore composite material based on high stability and highly acid micro porous molecular sieve Then there is important industrial application value.
With the continuous developing that molecular sieve catalytic is applied, the molecular sieve in single duct is no longer satisfied diversified urge Agent prepares demand.Micro porous molecular sieve is in heterogeneous catalysis application mainly with stronger Acidity and higher structural stability It is good at, but since micro porous molecular sieve mostly aperture is smaller, duct is elongated, and the macromolecular in reaction raw materials such as heavy oil is difficult to diffuse into Enter to inside duct, can then reduce the utilization rate of acidic site inside micro porous molecular sieve duct, while the duct of narrow elongate in this way Diffusional resistance is larger, and the quick diffusion for influencing reaction product molecule is overflowed, and is easy to cause drastic cracking and green coke.And mesoporous molecular Although sieve can make up the limitation that micro porous molecular sieve is spread in reactant and reaction product, the structure of mesopore molecular sieve is steady It is qualitative often poor, also limit its catalytic applications.
CN 200810012192 provides a kind of preparation method of Y molecular sieve/silicon dioxide composite material, by Y type molecule Sieve, sodium hydroxide, distilled water, template and silicon source are uniformly mixed under stirring, and reaction mixture gel, each component is made Mol ratio are as follows: (0-1.3) Na2O:(34.4-110)H2O:(0.75-11.3)SiO2: (0.046-0.7) R, R is template.It should Gel 12~70h of crystallization at 80-180 DEG C, is filtered, is washed, and hud typed composite material is obtained.Y molecular sieve is in composite wood Content in material is in 10~30wt%, and the partial size of composite material is at 2~10 μm.Y type molecular sieve is not involved in titanium dioxide in this method The outgrowth of silicon, without chemical bond between Y type molecular sieve and silica, silica cannot provide acidity, various It can only play the role of selecting type in catalysis reaction, so the acidity of composite material can only be realized by modulation Y molecular sieve.But it is mesoporous to be Irregular multi-stage porous.
Liu et al. is in document Journal of American Chemical Society (2000,122:8791-8792) Describe a kind of method for preparing mesoporous material using Y molecular sieve secondary structure unit: first by NaOH, NaAlO2, H2O and water Glass mixing, is made the Y molecular sieve seed-solution containing 27wt%SiO2 and 14wt%NaOH, template is introduced into seed-solution CTAB and dilution heat of sulfuric acid, the pH value for adjusting seed-solution is 9,100 DEG C of crystallization 20h, Y points in crystallization process in seed-solution Son sieve secondary structure unit is assembled into the composite material with hexagonal mesoporous structure, Al-MSU- under the action of template CTAB S.The purpose is to use the assembly mesoporous material of Y type molecular sieve, but the mesoporous wall of micro--mesoporous composite material is amorphous structure, Hydrothermal stability is poor.
Zhang etc. describes one kind in document Applied Catalysis A:General (2008,345:73-79) Y/MCM-48 is micro--preparation method of mesoporous composite material: NaY crystal seed is added in the precursor sol of MCM-48, presoma is molten Unclassified stores forms in liquid are as follows: 1TEOS:0.415CTAB:0.48NaOH:55H2O, after mixed liquor stirs 50 minutes, at 110 DEG C For a period of time, suction filtration, washing obtain solid product to lower hydrothermal crystallizing, and 550 DEG C of roasting 6h obtain Y/MCM-48 in air atmosphere Composite molecular screen.Although the mesoporous wall thickness of the MCM-48 molecular sieve of this method preparation is increased, its hole wall is still nothing Amorphous configuration, therefore poor be still of hydrothermal stability restricts its major reason applied.
CN102000604A provides one kind using kaolin as raw material, and inorganic silicate is to add silicon source, microwave method preparation The method of Y/MCM-41 composite molecular screen.Before adding a certain amount of sodium metasilicate synthesis Y type molecular sieve as raw material using kaolin first Body is driven, then using cetyl trimethylammonium bromide as template, microwave method prepares composite molecular screen Y/MCM-41.The Y/ of synthesis MCM-41 composite molecular screen has micro--mesoporous double-pore structure, and the specific surface area of sample is greater than 550m2/g, and average pore size is about 2.7nm, sample have regular hexagonal mesoporous structure.Although the MCM-41 molecular sieve hole wall of this method preparation introduces Y type Molecular sieve secondary structure unit, but thermal stability is still short of, and collapse temperature is lower than 800 DEG C.
CN101172244 provides a kind of preparation method of montmorillonite/Y molecular sieve composite material.By by montmorillonite Grain is uniformly mixed with Y molecular sieve gel, then carries out crystallization, and is filtered, washed and dried drying and the montmorillonite/Y molecule is made Sieve composite material.Composite material made from the method for the present invention, while there is the structure feature of montmorillonite and Y molecular sieve, montmorillonite With Y molecular sieve alternate, Y molecular sieve is grown on montmorillonite microballoon, but this method preparation composite material in Y molecular sieve skeleton Sial is relatively low, and it is poor to may cause its hydrothermal stability.
CN101172243 provides a kind of preparation method of mesoporous/micropore molecular sieve composite material.The composite material is logical It crosses to mix adobe isomery material (PCHs) with micro porous molecular sieve gel and carry out made from in-situ crystallization.Invention preparation In composite material, micro porous molecular sieve is wrapped in adobe isomery surrounding materials, which has micro porous molecular sieve simultaneously Crystal structure and adobe isomery material meso-hole structure, belong to porosity Composite material.Matched in composite material according to gel It can be crystallized to obtain the micro porous molecular sieves such as Y type, ZSM-5 type, β type than difference.The stability that this method prepares composite material is poor.
CN200610165597.0 provides a kind of preparation side of nano molecular sieve/sieve and silica-sesquioxide composite catalyzing material Method first synthesizes nano molecular sieve using directing agent method, and the precipitation step in synthesis is handled using microwave and/or ultrasonic wave, Then the mixture aqueous solution of waterglass and silicon source is added in the slurries containing nano molecular sieve, it is 7~9.5 that acid adding, which is adjusted to pH, Form gel;Then by gel drying, roasting to get the composite catalyzing material, wherein silicon source is selected from sodium metaaluminate or aluminum sulfate, The particle that this method sieves products molecule is maintained at 100nm or less and nano molecular sieve therein is not easy to assemble, without Acidic sol process and avoid molecular sieve by acid destroy.The composite material is suitable for the catalytic cracking of heavy oil macromolecular and hydrogen is added to split Change reaction.
Prndau etc. describes one in document Applied Catalysis A:General (1994,115:L7-L14) The method of kind fabricated in situ nano molecular sieve ZSM-5 in the duct of Silica hydrogel forms 3~5 μm of partial size in the outer surface of silica gel Zeolite, form 0.5~2 μm of partial size of zeolite in the macropore of silica gel, form partial size 0.02~0.035 in the mesoporous of silica gel μm zeolite.
Prndau etc. described in Chem.Mater (1999,11:2030-2037) it is a kind of by granular size be 10- The beta-molecular sieve of 15nm is stable at the method in Aluminum sol: being first dispersed in water gel aluminum hydroxide filter cake, pH=is made 9.05 aluminium hydroxide lotion: by the beta-molecular sieve slurries of its pH=12.7 at room temperature according to Al2O3/ molecular sieve=1:1 weight Than mixing, to pH=11.8, (dust technology is added after described mixing in the preparation of another two batches sample makes the pH for mixing rear slurry to amount Respectively 11.0 and 10.0);After stirring 2h, aging is for 24 hours at room temperature;Precipitating is isolated by decantation, and is dried in vacuo at 50 DEG C It is 70 weight % to water content.Extrusion granulation and in 120 DEG C of dry 5h, then temperature-programmed calcination.The disadvantages of the method are as follows system The standby time is longer.
The preparation method of the micro--mesoporous composite material referred in above-mentioned document or patent either process it is more complicated or The synthesis technology time is long.CN102000604A introduces microwave processing process during synthesizing Y/MCM-41 composite molecular screen, Ancillary equipment is increased, the cost for synthesizing composite molecular screen is increased considerably.In addition mentioned in document above or patent it is micro-- Mesoporous part in mesoporous composite material is irregular hole.In the above patent, heteropoly acid generally with the macropores such as aluminium oxide, sial without Amorphous configuration material load or mixing, but these materials, compared with regular mesoporous material, specific surface area is relatively low, drop The low catalytic reaction activity of heteropoly acid.Micro porous molecular sieve is since aperture is smaller, and heteropoly acid molecule is relatively large, after load It is larger that specific surface area and hole hold loss, it is difficult to play catalytic activity.The mesopore molecular sieve developed in recent years is greatly improved point Sub- sieve ratio surface area, Kong Rong and aperture, but there are thermostabilizations for the mesopore molecular sieves such as mesopore molecular sieve such as SBA-15 and MCM-41 Property it is poor, under long-time high-temperature condition, skeleton structure is easy to collapse, and is easy permanently to lose catalytic activity.
Summary of the invention
The purpose of the present invention is developing a kind of Y/SAPO-34/ZSM-11/ASA multilevel hole material, directed agents are synthesized first, Y/SAPO-34/ZSM-11 composite molecular screen is synthesized using hydrothermal crystallization method, then in the slurry of Y/SAPO-34/ZSM-11 molecular sieve Be added surfactant, alkaline silicon source and/or alkaline silicon source solution in liquid, product is washed, it is dry, roast to get mesoporous Y/ SAPO-34/ZSM-11/ASA composite material.
The present invention provides a kind of preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material, includes the following steps:
(1) directed agents are prepared:
Sodium hydroxide and silicon source are added to the water, or aluminium hydroxide is added to the water to after being completely dissolved and is added again Enter silicon source, forms sodium aluminate solution A, Al in solution A2O3Content be 2.5~10wt%, Na2O content is 8~35wt%; Solution A and water glass solution are added sequentially in deionized water under stiring, it is after mixing evenly, static old at 15~50 DEG C Change 0.5~60h, directed agents are made;The molar ratio of each component is Na in directed agents2O:Al2O3:SiO2:H2O=15~17:1:15 ~17:250~350;
(2) preparation of slurries D:
According to SAPO-34 molecular sieve: ZSM-11 molecular sieve: aqueous solution mass ratio is 1:0.2~5:3~7, by SAPO- 34 and ZSM-11 molecular sieve disperses in aqueous solution, to be heated to 70~80 DEG C, and constant temperature stirs 2~5h, obtains SAPO-34 and ZSM- 11 molecular sieve pulps adjust the pH value of SAPO-34 and ZSM-11 molecular sieve pulp, obtain SAPO-34 and ZSM-11 molecule screening the pulp Liquid D;
The aqueous solution is the aqueous solution of 1~10wt% potassium hydroxide and 1~5wt% boric acid;
(3) preparation of Y/SAPO-34/ZSM-11 composite molecular screen slurries E:
Silicon source is dissolved in water, Al is formed2O3Content is the solution B of 1~4wt%;
Sodium hydroxide is added to the water with silicon source or aluminium hydroxide is added to the water to after being completely dissolved and adds aluminium Source forms sodium aluminate solution C, Al in solution C2O3Content be 3~9wt%, Na2O content is 1~20wt%;
The directed agents, solution B, solution C and slurries D are added to, synthesis NaY molecular sieve is made in water glass solution Reaction mixture;By the weight of reaction mixture for 100wt% in terms of, the additional amounts of directed agents is 0.5~20wt%, is synthesized The molar ratio of the reaction mixture each component of NaY are as follows: Na2O:Al2O3:SiO2:H2O=4~8:1:10~15:200~300;
After reaction mixture crystallization, Y/SAPO-34/ZSM-11 composite molecular screen slurries E is obtained;
(4) preparation of Y/SAPO-34/ZSM-11/ASA multilevel hole material
Surfactant is added in the Y/SAPO-34/ZSM-11 composite molecular screen slurries E, alkaline silicon source is added Or alkaline silicon source solution, and it is adjusted with acid the pH value of system, finally obtained solid mixture matter is filtered, washed, dry, is roasted It burns, obtains Y/SAPO-34/ZSM-11/ASA multilevel hole material.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: in step (4), The surfactant is preferably at least one of CTAB, P123 and F127.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: in step (4), The additional amount of the surfactant is preferably the 1~3wt% for accounting for Y/SAPO-34/ZSM-11/ASA multilevel hole material weight.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: in step (2), The pH value is preferably 7~8.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: in step (4), The pH value is preferably 7~9.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: in step (3), The condition of crystallization is preferred are as follows: 8~48h of crystallization at 80~140 DEG C.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: step (1) with (3) in, source of aluminium is preferably sodium metaaluminate, boehmite, boehmite, aluminum nitrate, aluminum sulfate, aluminium hydroxide and three water One or more of aluminium stone.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: in step (4), The alkalinity silicon source is preferably sodium metaaluminate, or the boehmite, boehmite, the hydroxide that are dissolved in sodium hydroxide solution Aluminium or gibbsite.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: in step (4), The acid is preferably sulfuric acid, hydrochloric acid or nitric acid.
The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material of the present invention, in which: the Y/SAPO- Mesoporous mesoporous for rule in 34/ZSM-11/ASA multilevel hole material, total pore volume is 0.52~0.62mL/g, and Micropore volume is 0.20~0.30mL/g, mesoporous 0.27~0.40mL/g of Kong Rongwei.
The present invention can be with details are as follows:
A kind of Y/SAPO-34/ZSM-11/ASA multilevel hole material preparation method, voluminous heavy naphtha and kerosene hydrogenation cracking Catalyst preparation includes the following steps:
1, directed agents are prepared: sodium hydroxide and silicon source are added to the water, or sodium hydroxide are added to the water molten Silicon source is added after solution, forms sodium aluminate solution A, Al in solution A2O3Content be 3.8wt%, Na2O content is 20wt%; Solution A is added in water glass solution under stiring, after mixing evenly, directed agents are made in the static ageing 3h at 30 DEG C;It leads Into agent, the molar ratio of each component is 16Na2O:Al2O3:16SiO2:330H2O。
2, prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: aqueous solution Ratio is 1:1:5, SAPO-34 and ZSM-11 molecular sieve is dispersed in 1~10wt% potassium hydroxide and 1~5wt% boric acid, is added For heat to 70~80 DEG C, constant temperature stirs 2h, obtains SAPO-34 and ZSM-11 molecular sieve pulp, pH value is adjusted to 7~8, is obtained SAPO-34 and ZSM-11 molecular sieve pulp D.
3, the preparation of Y/SAPO-34/ZSM-11/ASA: water-soluble silicon source is dissolved in water, and forms Al2O3Content is The solution B of 2wt%;Sodium hydroxide is added to the water with silicon source or sodium hydroxide is added to the water after dissolution and adds aluminium Source forms sodium aluminate solution C, Al in solution C2O3Content be 6.5wt%, Na2O content is 13.2wt%;By directed agents, Solution B, solution C and slurries D are added to the reaction mixture that synthesis NaY molecular sieve is made in water glass solution;To react mixing The weight of object is 100wt% meter, and the additional amount of directed agents is 6wt%, obtains the reaction mixture of synthesis NaY, obtains synthesis NaY Reaction mixture each component molar ratio are as follows: 6.2Na2O:Al2O3:12SiO2:260H2O mixes the reaction of NaY molecular sieve Object crystallization 22h at 105 DEG C obtains Y/SAPO-34/ZSM-11 composite molecular screen slurries E.A certain amount of surfactant (is accounted for 1~6wt% of ASA weight) be added in Y/SAPO-34/ZSM-11 molecular sieve pulp E, be added while stirring alkaline silicon source or Alkaline silicon source solution, and the pH value for being adjusted with acid system is 7~9, finally filters solid mixture matter obtained above, washes It washs, 100 DEG C of dry 4h, 550 DEG C of roasting 6h, obtains mesoporous Y/SAPO-34/ZSM-11/ASA composite material.
Surfactant of the present invention mainly has tri- kinds of nonionic surfactants of CTAB, P123 and F127.
The silicon source used in the preparation process of Y/SAPO-34/ZSM-11/ASA composite material of the present invention is that this field is normal , such as water glass solution.
Silicon source used in Y/SAPO-34/ZSM-11/ASA composite material preparation process of the present invention is this field Commonly, such as sodium metaaluminate, boehmite, boehmite, aluminum nitrate, aluminum sulfate, aluminium hydroxide and/or gibbsite, alkali Property silicon source be it is commonly used in the art, aluminium therein from sodium metaaluminate or can be dissolved in sodium hydroxide solution and intend thin water aluminium Stone, boehmite, aluminium hydroxide, gibbsite, alkaline silicon source be it is commonly used in the art, silicon therein can derive from waterglass. Acid is acid generally in the art, preferably inorganic acid, such as sulfuric acid, hydrochloric acid, nitric acid.
The content of Y molecular sieve is 10~80wt% in Y/SAPO-34/ZSM-11/ASA composite material of the present invention, The content of SAPO-34 molecular sieve is 1~5wt%, and the content of ZSM-11 molecular sieve is 1~5wt%, remaining is sieve and silica-sesquioxide (SiO2/Al2O3) and Al2O3、SiO2One of, the SiO of sieve and silica-sesquioxide2With Al2O3Molar ratio be preferably 1:1~10:1.
NaY molecular sieve differential thermal fail temperature is reachable in Y/SAPO-34/ZSM-11/ASA composite material of the present invention 1008~1100 DEG C, the mesoporous average pore size of rule is 3~10nm, and total pore volume is 0.52~0.62mL/g, and Micropore volume is 0.20~0.30mL/g, mesoporous 0.27~0.40mL/g of Kong Rongwei.
In conclusion NaY molecular sieve has crystal grain small in Y/SAPO-34/ZSM-11 composite molecular screen produced by the present invention (100~400nm), framework si-al ratio are high, thermal stability improve (5 DEG C higher than the differential thermal fail temperature of corresponding NaY molecular sieve with On) and the mesoporous composition of rule less than the micropore of 1nm and 3~10nm micro--composite mesoporous pore structure the characteristics of.
Specific embodiment
Elaborate below to the embodiment of the present invention: the present embodiment carries out under the premise of the technical scheme of the present invention Implement, gives detailed embodiment and process, but protection scope of the present invention is not limited to following embodiments, following implementation Test method without specific conditions in example, usually according to normal condition.
Analysis test method:
The measurement of the relative crystallinity and framework si-al ratio of NaY molecular sieve: using the production of Bruker company of Germany D8Advance X-ray diffractometer, determination condition are as follows: CuK α radiation, pipe press 40kV, tube current 40mA.Its measuring method according to SH/T 0340-92 standard method measurement (see " standard of chemical industry compilation ", China Standards Press publishes for 2000), bone The measurement of frame silica alumina ratio be by SH/T 0399-92 standard method, (see " standard of chemical industry compilation ", China Standards Press, 2000 publish) measurement and according to the following formula:
Calculate the lattice constant a of NaY molecular sieve.
Then according to Breck-FPrnigen formula:
Calculate the framework si-al ratio of NaY molecular sieve.
Sem analysis uses the 435VP type scanning electron microscope of Britain LEO company production, acceleration voltage 20kV, sample It is gold-plated with physical method before testing.
Thermal stability determination carries out on German Nai Chi instrument company STA 409PC type thermal analyzer.Experiment is in Ar atmosphere Middle progress, heating rate are 10 DEG C/min, temperature range: room temperature~1200 DEG C.
Specific surface area and hole hold test: the measurement of the specific surface area and pore structure of catalyst and molecular sieve exists It is carried out in the ASAP2020M specific surface and lacunarity analysis instrument of the production of Micromeritics company, according to BET method calculating ratio table Area;BJH method calculated pore.
The synthesis of embodiment 1:Y/SAPO-34/ZSM-11/ASA composite material
(1) it the preparation of directed agents: takes 24.7g sodium hydroxide (Beijing Chemical Plant analyzes pure) to be added in 45.9g water, stirs It mixes to sodium hydroxide and all dissolves, add 6.5g sodium metaaluminate (research institute of Shandong Aluminium Industrial Corp, industrial goods, Al2O3Content 49.1wt%), stirring is all dissolved to sodium metaaluminate, obtains sodium aluminate solution A.By 70g solution A and 100g waterglass (Beijing Red Star water glass plant, SiO2Content 27.81wt%, Na2O content 8.74wt%) it successively pours into 65.5g deionized water, stirring is equal After even at 30 DEG C static ageing 22h, obtain directed agents.The molar ratio of directed agents each component are as follows: 16Na2O:Al2O3:16SiO2: 330H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:1:5, by the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 2g be dispersed in 10g 5wt% potassium hydroxide and In the aqueous solution of 5wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, SAPO-34 and ZSM-11 molecular sieve pulp is obtained, Slurry pH value is adjusted to 7~8, SAPO-34 and ZSM-11 molecular sieve pulp D is obtained.
(3) preparation of Y/SAPO-34/ZSM-11 molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3 Content is the aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (specification is same Step 1), stirring form sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to Conventional NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g in step 1) again after mixing evenly The reaction mixture of synthesis NaY molecular sieve is made in water.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will Reaction mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, and it is compound to obtain Y/SAPO-34/ZSM-11 Molecular sieve pulp E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal Fail temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 0.8g sodium hydroxide is dissolved in 6.2g water, then 1g sodium metaaluminate is added, stirring to sodium metaaluminate is all dissolved, and solution F is obtained.The Y/SAPO-34/ZSM-11 that step (3) is obtained Molecular sieve and mother liquor are cooled to room temperature, and are transferred in beaker, static layering, upper layer mother liquor 32mL are taken out, then to Y/SAPO- Surfactant P123 0.8g is added in the mix suspending object of 34/ZSM-11 molecular sieve and mother liquor and is stirred at 20 DEG C Solution F is added in 30min later, continues to stir 1h after adding, sulfuric acid is added in the mixture of above-mentioned stirring, regulation system PH value be 7.Finally solid matter obtained above is filtered, washed, 120 DEG C of dry 12h, 500 DEG C of roasting 4h, obtains Y/ SAPO-34/ZSM-11/ASA composite material, intermediary hole part are sieve and silica-sesquioxide, and the molar ratio of sieve and silica-sesquioxide is 8.5: 1, mesoporous is mesoporous, the aperture 5nm of rule, and the content of Y molecular sieve is 62wt%.Y/SAPO-34/ZSM-11/ASA composite material The differential thermal fail temperature of middle NaY molecular sieve is 1010 DEG C, and texture property is shown in Table 1.
Embodiment 2
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 28.7g sodium hydroxide to be added in 45.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 100g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 17Na2O:Al2O3:16SiO2:330H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:0.5:7, and the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 1g is dispersed in the 6wt% potassium hydroxide of 14g In the aqueous solution of 5wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, obtains SAPO-34 and ZSM-11 molecule screening the pulp Slurry pH value is adjusted to 7~8, obtains SAPO-34 and ZSM-11 molecular sieve pulp D by liquid.
(3) preparation of Y/SAPO-34/ZSM-11 molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3 Content is the aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (specification is same Step 1), stirring form sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to Conventional NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g in step 1) again after mixing evenly The reaction mixture of synthesis NaY molecular sieve is made in water.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will Reaction mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, and it is compound to obtain Y/SAPO-34/ZSM-11 Molecular sieve pulp E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal Fail temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 7.5g sodium hydroxide is dissolved in 58g water, then 9.2g sodium metaaluminate is added, stirring to sodium metaaluminate is all dissolved, and solution F is obtained.The Y/SAPO-34/ZSM- that step (3) is obtained 11 molecular sieves and mother liquor are cooled to room temperature, and are transferred in beaker, at 25 DEG C, sequentially add P123 1.6g, water glass while stirring Glass 7.8g and solution F.Continue to stir 2h at 25 DEG C, nitric acid solution is added in the mixture of above-mentioned stirring, finally makes body The pH value of system is 8.5.Finally solid matter obtained above is filtered, washed, 150 DEG C of dry 4h, 450 DEG C of roasting 10h, is obtained Y/SAPO-34/ZSM-11/ASA composite material, intermediary hole part are sieve and silica-sesquioxide, and the molar ratio of sieve and silica-sesquioxide is 5: 1, mesoporous is mesoporous, the aperture 8nm of rule, and the content of Y molecular sieve is 35wt%.Y/SAPO-34/ZSM-11/ASA composite material The differential thermal fail temperature of middle NaY molecular sieve is 1008 DEG C, and texture property is shown in Table 1.
Embodiment 3
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 20.7g sodium hydroxide to be added in 45.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 93g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 15Na2O:Al2O3:15SiO2:330H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:0.75:3, and the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 1.5g is dispersed in the 7wt% hydroxide of 6g In the aqueous solution of potassium and 5wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, obtains SAPO-34 and ZSM-11 molecule screening the pulp Slurry pH value is adjusted to 7~8, obtains SAPO-34 and ZSM-11 molecular sieve pulp D by liquid.
(3) preparation of Y/SAPO-34/ZSM-11 molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3 Content is the aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (specification is same Step 1), stirring form sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to Conventional NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g in step 1) again after mixing evenly The reaction mixture of synthesis NaY molecular sieve is made in water.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will Reaction mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, and it is compound to obtain Y/SAPO-34/ZSM-11 Molecular sieve pulp E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal Fail temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 3.6g sodium hydroxide is dissolved in 27.6g water, 16.1g sodium metaaluminate is added, stirring to sodium metaaluminate is all dissolved, and solution F is obtained.The Y/SAPO-34/ that step (3) is obtained ZSM-11 molecular sieve and mother liquor are cooled to room temperature, and mother liquor 90mL are taken out, then by remaining mother liquor and Y/SAPO-34/ZSM-11 In the beaker that the mixture of molecular sieve is transferred to, CTAB 6.5g and solution F is added while stirring at 18 DEG C, after adding solution F Continue to stir 4h at 18 DEG C, hydrochloric acid solution is added in the mixture of above-mentioned stirring, the pH value of regulation system is 7.8.Finally Solid matter obtained above is filtered, washed, 110 DEG C of dry 32h, 550 DEG C of roasting 6h, obtains Y/SAPO-34/ZSM-11/ ASA composite material, intermediary hole part are sieve and silica-sesquioxide, and the molar ratio of sieve and silica-sesquioxide is 4.5:1, mesoporous to be situated between for rule Hole, aperture 5.5nm, the content of Y type molecular sieve are 60wt%.NaY molecule in Y/SAPO-34/ZSM-11/ASA composite material The differential thermal fail temperature of sieve is 1020 DEG C, and texture property is shown in Table 1.
Embodiment 4
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 24.7g sodium hydroxide to be added in 30.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 107g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 16Na2O:Al2O3:17SiO2:300H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:0.5:5, and the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 1g is dispersed in the 6wt% potassium hydroxide of 10g In the aqueous solution of 4wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, obtains SAPO-34 and ZSM-11 molecule screening the pulp Slurry pH value is adjusted to 7~8, obtains SAPO-34 and ZSM-11 molecular sieve pulp D by liquid.
(3) preparation of Y/SAPO-34/ZSM-11 molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3 Content is the aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (specification is same Step 1), stirring form sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to Conventional NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g in step 1) again after mixing evenly The reaction mixture of synthesis NaY molecular sieve is made in water.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will Reaction mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, and it is compound to obtain Y/SAPO-34/ZSM-11 Molecular sieve pulp E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal Fail temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 3.6g sodium hydroxide is dissolved in 37.6mL water, 4.4g aluminium hydroxide is added, stirring to aluminium hydroxide is all dissolved, and solution F is obtained.The Y/ containing mother liquor that step (3) is obtained SAPO-34/ZSM-11 molecular sieve filtration, washing to washing water pH value be 9, then Y/SAPO-34/ZSM-11 molecular sieve is added Water mashing, is added CTAB 4.8g while stirring at 20 DEG C, stirs 30min, then solution F and sulfuric acid, the pH value of regulation system It is 8.0.Finally mixture obtained above is filtered, washed, 125 DEG C of dry 16h, 600 DEG C of roasting 3h obtain Y/SAPO-34/ ZSM-11/ASA composite material.Its intermediary hole part is sieve and silica-sesquioxide, and the molar ratio of sieve and silica-sesquioxide is 5.5:1, mesoporous to be Mesoporous, the aperture 3.5nm of rule, the content of Y type molecular sieve are 60wt%.In Y/SAPO-34/ZSM-11/ASA composite material 1105 DEG C of the differential thermal fail temperature of NaY molecular sieve, texture property is shown in Table 1.
Embodiment 5
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 24.7g sodium hydroxide to be added in 55.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 100g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 16Na2O:Al2O3:16SiO2:350H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:0.5:7, and the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 1g is dispersed in the 8wt% potassium hydroxide of 14g In the aqueous solution of 5wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, obtains SAPO-34 and ZSM-11 molecule screening the pulp Slurry pH value is adjusted to 7~8, obtains SAPO-34 and ZSM-11 molecular sieve pulp D by liquid.
(3) preparation of Y/SAPO-34/ZSM-11 molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3 Content is the aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (specification is same Step 1), stirring form sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to Conventional NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g in step 1) again after mixing evenly The reaction mixture of synthesis NaY molecular sieve is made in water.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will Reaction mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, and it is compound to obtain Y/SAPO-34/ZSM-11 Molecular sieve pulp E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal Fail temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 99.6g waterglass is poured into 171.4mL water, is obtained Solution F.It is by the Y/SAPO-34/ZSM-11 molecular sieve filtration containing mother liquor that step (3) obtains, washing to the pH value of washing water 9, then add water to be beaten in Y/SAPO-34/ZSM-11 molecular sieve, the F127 and solution F of 3.8g is added while stirring at 20 DEG C, It is 8.0 with the pH value of sulfuric acid regulation system.Finally compounding substances obtained above are filtered, washed, 120 DEG C of dry 10h, 550 DEG C roasting 5h, obtains Y/SAPO-34/ZSM-11/ASA composite material, the molar ratio of sieve and silica-sesquioxide is 4.5:1, mesoporous for rule Then mesoporous, aperture 6.5nm, the content of Y type molecular sieve is 65wt%.NaY in Y/SAPO-34/ZSM-11/ASA composite material 1008 DEG C of the differential thermal fail temperature of molecular sieve, texture property is shown in Table 1.
Embodiment 6
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 24.7g sodium hydroxide to be added in 45.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 100g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 16Na2O:Al2O3:16SiO2:330H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:0.75:3, and the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 1.5g is dispersed in the 8wt% hydroxide of 6g In the aqueous solution of potassium and 5wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, obtains SAPO-34 and ZSM-11 molecule screening the pulp Slurry pH value is adjusted to 7~8, obtains SAPO-34 and ZSM-11 molecular sieve pulp D by liquid.
(3) preparation of NaY type molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3Content is The aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (the same step of specification 1), stirring forms sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to routine NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g water in step 1) again after mixing evenly, makes At the reaction mixture of synthesis NaY molecular sieve.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will reaction Mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, obtains Y/SAPO-34/ZSM-11 compound molecule Screening the pulp liquid E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal destroy Temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 3.6g sodium hydroxide is dissolved in 27.6g water, 4.4g sodium metaaluminate is added, stirring to sodium metaaluminate is all dissolved, and solution F is obtained.The Y/SAPO-34/ that step (3) is obtained ZSM-11 molecular sieve and mother liquor are cooled to room temperature, and mother liquor 180mL are taken out, then by remaining mother liquor and Y/SAPO-34/ZSM-11 The mixture of molecular sieve is transferred in plastic beaker, sequentially added while stirring at 30 DEG C P123 1.3g, SAPO-34 with ZSM-11 molecular sieve pulp E, solution D and sulfuric acid, the pH value of regulation system are 7.5.Finally by solid mixture obtained above Matter is filtered, washed, 130 DEG C of dry 8h, 650 DEG C of roasting 4h, obtains Y/SAPO-34/ZSM-11/ASA composite material, intermediary hole Part is sieve and silica-sesquioxide, and the silica alumina ratio of sieve and silica-sesquioxide is 2.5:1, and mesoporous is mesoporous, the aperture 9.5nm of rule, with On the basis of Y/SAPO-34/ZSM-11/ASA composite material, the content of Y type molecular sieve is 80wt%.Y/SAPO-34/ZSM-11/ 1055 DEG C of the differential thermal fail temperature of NaY molecular sieve in ASA composite material, texture property is shown in Table 1.
Embodiment 7
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 24.7g sodium hydroxide to be added in 35.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 100g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 16Na2O:Al2O3:16SiO2:300H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:1:7, by the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 2g be dispersed in 14g 9wt% potassium hydroxide and In the aqueous solution of 4wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, SAPO-34 and ZSM-11 molecular sieve pulp is obtained, Slurry pH value is adjusted to 7~8, SAPO-34 and ZSM-11 molecular sieve pulp D is obtained.
(3) preparation of NaY type molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3Content is The aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (the same step of specification 1), stirring forms sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to routine NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g water in step 1) again after mixing evenly, makes At the reaction mixture of synthesis NaY molecular sieve.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will reaction Mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, obtains Y/SAPO-34/ZSM-11 compound molecule Screening the pulp liquid E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal destroy Temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 3.6g sodium hydroxide is dissolved in 27.6g water, 8.8g sodium metaaluminate is added, stirring to sodium metaaluminate is all dissolved, and solution F is obtained.The Y/SAPO-34/ that step (3) is obtained ZSM-11 molecular sieve and mother liquor are cooled to room temperature, and mother liquor 200mL are taken out, then by remaining mother liquor and Y/SAPO-34/ZSM-11 The mixture of molecular sieve is transferred in beaker, and P123 0.8g and F127 4.2g is added while stirring at 25 DEG C and stirs evenly Afterwards, solution F and sulfuric acid are sequentially added, the pH value of regulation system is 8.0.Finally solid matter obtained above is filtered, is washed It washs, 120 DEG C of dry 12h, 550 DEG C of roasting 4h, obtains Y/SAPO-34/ZSM-11/ASA composite material, intermediary hole part is silicon Aluminum oxide, the silica alumina ratio of sieve and silica-sesquioxide are 1.5:1, and mesoporous is mesoporous, the aperture 9.2nm, with Y/SAPO- of rule On the basis of 34/ZSM-11/ASA composite material, the content of Y type molecular sieve is 80wt%.Y/SAPO-34/ZSM-11/ASA is compound 1027 DEG C of the differential thermal fail temperature of NaY molecular sieve in material, texture property is shown in Table 1.
Embodiment 8
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 24.7g sodium hydroxide to be added in 45.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 100g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 16Na2O:Al2O3:16SiO2:330H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:0.5:3, and the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 1g is dispersed in the 10wt% potassium hydroxide of 6g In the aqueous solution of 2wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, obtains SAPO-34 and ZSM-11 molecule screening the pulp Slurry pH value is adjusted to 7~8, obtains SAPO-34 and ZSM-11 molecular sieve pulp D by liquid.
(3) preparation of NaY type molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3Content is The aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (the same step of specification 1), stirring forms sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to routine NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g water in step 1) again after mixing evenly, makes At the reaction mixture of synthesis NaY molecular sieve.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will reaction Mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, obtains Y/SAPO-34/ZSM-11 compound molecule Screening the pulp liquid E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal destroy Temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 3.6g sodium hydroxide is dissolved in 27.6g water, 8.8g sodium metaaluminate is added, stirring to sodium metaaluminate is all dissolved, and solution F is obtained.The Y/SAPO-34/ that step (3) is obtained ZSM-11 molecular sieve and mother liquor are cooled to room temperature, and mother liquor 220mL are taken out, then by remaining mother liquor and Y/SAPO-34/ZSM-11 The mixture of molecular sieve is transferred in beaker, and P123 1.2g and CTAB 3.8g is added while stirring at 25 DEG C, stirs evenly Afterwards, solution F and sulfuric acid are sequentially added, the pH value of regulation system is 8.0.Finally solid matter obtained above is filtered, is washed It washs, 120 DEG C of dry 12h, 550 DEG C of roasting 4h, obtains Y/SAPO-34/ZSM-11/ASA composite material, intermediary hole part is silicon Aluminum oxide, the silica alumina ratio of sieve and silica-sesquioxide are 1:1, and mesoporous mesoporous for rule, aperture 7.5nm, Y type molecular sieve contains Amount is 80wt%.1034 DEG C of the differential thermal fail temperature of NaY molecular sieve, texture in Y/SAPO-34/ZSM-11/ASA composite material Matter is shown in Table 1.
Embodiment 9
Except special instruction, each raw material sources are the same as embodiment 1.
(1) preparation of directed agents: taking 24.7g sodium hydroxide to be added in 55.9g water, stirs all molten to sodium hydroxide Solution adds 6.5g sodium metaaluminate, and stirring to sodium metaaluminate is all dissolved, and obtains sodium aluminate solution A.By 70g solution A and 100g Waterglass successively pours into 65.5g deionized water, and the static ageing 22h at 30 DEG C, obtains directed agents after mixing evenly.Directed agents are each The molar ratio of component are as follows: 16Na2O:Al2O3:16SiO2:350H2O。
(2) prepared by SAPO-34 and ZSM-11 molecular sieve pulp: according to SAPO-34 molecular sieve: ZSM-11 molecular sieve: water-soluble Liquid proportional is 1:1:5, by the ZSM-11 molecular sieve of the SAPO-34 molecular sieve of 2g and 2g be dispersed in 10g 5wt% potassium hydroxide and In the aqueous solution of 5wt% boric acid, 70~80 DEG C are heated to, constant temperature stirs 2h, SAPO-34 and ZSM-11 molecular sieve pulp is obtained, Slurry pH value is adjusted to 7~8, SAPO-34 and ZSM-11 molecular sieve pulp D is obtained.
(3) preparation of NaY type molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3Content is The aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (the same step of specification 1), stirring forms sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B, solution C and slurries D according to routine NaY molecular sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g water in step 1) again after mixing evenly, makes At the reaction mixture of synthesis NaY molecular sieve.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;It will reaction Mixture is gone in autoclave, and crystallization 22h, hydrothermal crystallizing finish at 105 DEG C, obtains Y/SAPO-34/ZSM-11 compound molecule Screening the pulp liquid E.Wherein the relative crystallinity of NaY molecular sieve be 95%, framework si-al ratio 5.2, partial size 200nm, differential thermal destroy Temperature is 950 DEG C.
(4) preparation of Y/SAPO-34/ZSM-11/ASA composite material: 3.6g sodium hydroxide is dissolved in 27.6g water, 8.8g sodium metaaluminate is added, stirring to sodium metaaluminate is all dissolved, and solution F is obtained.The Y/SAPO-34/ that step (2) is obtained ZSM-11 molecular sieve and mother liquor are cooled to room temperature, and mother liquor 200mL are taken out, then by remaining mother liquor and Y/SAPO-34/ZSM-11 The mixture of molecular sieve is transferred in plastic beaker, CTAB 4.2g and F127 8.2g is added while stirring at 25 DEG C, successively Solution F and sulfuric acid is added, the pH value of regulation system is 8.0.Finally solid matter obtained above is filtered, washed, 120 DEG C it is dry Dry 12h, 550 DEG C of roasting 4h obtain Y/SAPO-34/ZSM-11/ASA composite material, and intermediary hole part is sieve and silica-sesquioxide, The silica alumina ratio of sieve and silica-sesquioxide is 1.5:1, and mesoporous mesoporous for rule, the content of aperture 7.3nm, Y type molecular sieve are 70wt%.1050 DEG C of the differential thermal fail temperature of NaY molecular sieve in Y/SAPO-34/ZSM-11/ASA composite material, texture property is shown in Table 1.
Comparative example 1
P123 is not added using the condition of embodiment 1, but when preparing Y/ASA composite material.
(1) it the preparation of directed agents: takes 24.7g sodium hydroxide (Beijing Chemical Plant analyzes pure) to be added in 45.9g water, stirs It mixes to sodium hydroxide and all dissolves, add 6.5g sodium metaaluminate (research institute of Shandong Aluminium Industrial Corp, industrial goods, Al2O3Content 49.1wt%), stirring is all dissolved to sodium metaaluminate, obtains sodium aluminate solution A.By 70g solution A and 100g waterglass (Beijing Red Star water glass plant, SiO2Content 27.81wt%, Na2O content 8.74wt%) it successively pours into 65.5g deionized water, stirring is equal After even at 30 DEG C static ageing 22h, obtain directed agents.The molar ratio of directed agents each component are as follows: 16Na2O:Al2O3:16SiO2: 330H2O。
(2) preparation of NaY type molecular sieve: 14.5g aluminum sulfate is dissolved in 50.6g water, forms Al2O3Content is The aluminum sulfate solution B of 3.4wt%;4.5g sodium hydroxide is dissolved in 50.4g water, then plus 10g sodium metaaluminate (the same step of specification 1), stirring forms sodium aluminate solution C to being completely dissolved.By 10.3g directed agents, solution B and solution C according to conventional NaY molecule Sieve preparation step is added sequentially to 75g waterglass, and (specification adds 48.5g water again after mixing evenly, synthesis is made in step 1) The reaction mixture of NaY molecular sieve.The molar ratio of each component is 6.2Na2O:Al2O3:12SiO2:260H2O;By reaction mixture It goes in autoclave, the crystallization 22h at 105 DEG C.Hydrothermal crystallizing finishes, and takes out molecular sieve and mother liquor, is filtered, washed, dries, i.e., Obtain NaY type zeolite product.
The relative crystallinity of gained NaY molecular sieve is 95%, framework si-al ratio 5.2, partial size 200nm, and differential thermal destroys Temperature is 950 DEG C.
(3) preparation of Y/ASA composite material: in addition to surfactant is not added, with (4) the step of embodiment 1.Mesoporous hole Diameter is 3.3~5.2nm.910 DEG C of the differential thermal fail temperature of NaY molecular sieve in Y/ASA composite material, texture property is shown in Table 1.
Comparative example 2
Small crystal grain NaY molecular sieve is prepared by the method for the embodiment 1 of CN 1033503C and prepares Y/ASA composite material.
(1) preparation of directed agents: taking 29.5g sodium hydroxide to be added in 75g water, and stirring to sodium hydroxide is all dissolved, 4.78g boehmite is added, stirring to boehmite is all dissolved, and sodium metaaluminate is obtained.200g waterglass is added to 1h is mixed in the sodium metaaluminate and 12g deionized water of above-mentioned preparation at 35 DEG C, is then made and rubs in 35 DEG C of static aging 6h You are than being 16Na2O:Al2O3:15SiO2:320H2O, the conventional directed agents of light transmittance < 30%.
189g specification waterglass same as described above is added in conventional directed agents, after placing 1.5h at 30 DEG C, is made Light transmittance is 90%, and mole group becomes 20.6Na2O:Al2O3:30SiO2:495H2O as clear as crystal improvement directing agent solution, It is placed at room temperature for and uses afterwards for 24 hours.
(2) preparation of NaY type molecular sieve: according to molar ratio 3.84Na2O:Al2O3:12SiO2:220H2The synthesizing formula of O, By 250g specification waterglass same as described above, the improvement directed agents of the above-mentioned preparation of 510g, 160g Al2O3Content is 6.8wt% Aluminum sulfate solution and 9.7g sodium aluminate solution (Al2O3Content 7.5wt%, Na2O content is 15wt%) 1h is mixed, so After be warming up to 97 DEG C, crystallization 26h, it is filtering, dry.
The relative crystallinity of gained NaY molecular sieve is 79%, framework si-al ratio 5.8, partial size 100nm, and differential thermal destroys Temperature is 935 DEG C.
(3) preparation of Y/ASA composite material: with (4) the step of embodiment 4, CTAB is not added.Mesoporous part is sial oxygen Compound, silica alumina ratio 5.5:1, mesoporous aperture are 3.2~6.5nm, and the differential thermal of NaY molecular sieve destroys in Y/ASA composite material 1050 DEG C of temperature, texture property is shown in Table 1.
Comparative example 3
By the method synthesis NaY molecular sieve that CN 201010514225.0 is provided and prepare Y/ASA composite material.
(1) synthesize directed agents: take 48g waterglass (modulus 3.0), add 8g polyethylene glycol PEG-2000, at 15 DEG C with 200 revs/min of mixing speed stirs 1h, obtains solution A;7.8g sodium hydroxide is dissolved in 24mL water, meta-aluminic acid is added Sodium 1.6g, stirring to sodium metaaluminate are all dissolved, and solution B is obtained;Solution A is stirred under 3000 revs/min of mixing speed, it will Solution B is poured into solution A, and 1.5h is stirred in continuation under 3000 revs/min of mixing speeds, finally with 200 revs/min at 15 DEG C Mixing speed stirs aging 12h, and 20.4mL water is supplemented after aging, continues to stir at 15 DEG C with 200 revs/min of mixing speeds 0.5h.In addition to PEG-2000, the molar ratio of remaining each component is 18Na2O:Al2O3:22SiO2:426H2O.It is spare to place 10h.
(2) it synthesizes NaY type molecular sieve: 3g sodium hydroxide being dissolved in 23.3mL water, 3.7g sodium metaaluminate is added, stirs It mixes to sodium metaaluminate and all dissolves, 10.5g polyethylene glycol 2000 (PEG-2000) is added under stiring to whole dissolutions, obtains solution C;15g aluminum sulfate is dissolved in 25mL water, solution D is obtained.C solution is stirred with 3000 revs/min of mixing speed, is sequentially added Water glass solution 90g, directed agents 10.6g, solution D and solution C, obtain colloidal sol E.Colloidal sol E is stirred at 15 DEG C with 3000 revs/min It mixes speed to stir 20 minutes, then stirs 1h with 200 revs/min of mixing speeds, obtain colorless gel.Obtained colorless gel is turned It moves on in the synthesis reactor of inner liner polytetrafluoroethylene, the hydrothermal crystallizing 32h at 104 DEG C obtains NaY type molecular sieve.
The relative crystallinity of gained nano NaY molecular sieve is 82%, framework si-al ratio 5.0, partial size are 20~100nm, Differential thermal fail temperature is 900 DEG C.
(3) preparation of Y/ASA composite material: with (4) the step of embodiment 2, P123 is not added.Mesoporous part is sial oxygen Compound, silica alumina ratio 5:1, mesoporous aperture are 6.2~8.2nm, and the differential thermal of NaY molecular sieve destroys temperature in Y/ASA composite material 985 DEG C of degree, texture property is shown in Table 1.
The texture property of NaY in table 1Y/SAPO-34/ZSM-5/ASA composite material
The Y/SAPO-34/ZSM-11/ASA composite wood prepared it can be seen from the result of table 1 using method of the invention The differential thermal fail temperature of NaY molecular sieve in material is improved.Y/SAPO-34/ZSM-11/ASA prepared by the present invention is multiple Condensation material has biggish total pore volume and mesoporous Kong Rong, and mesoporous average pore size is 3~10nm and is regular meso-hole structure, to have The conversion of machine macromolecular provides open space, is conducive to the Efficient Conversion of heavy oil molecules.And in composite material preparation process, The random distribution of mesoporous pore size of composite material for being not added with surface-active and preparing.

Claims (10)

1. a kind of preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material, includes the following steps:
(1) directed agents are prepared:
Sodium hydroxide and silicon source are added to the water, or aluminium hydroxide is added to the water to after being completely dissolved and adds aluminium Source forms sodium aluminate solution A, Al in solution A2O3Content be 2.5~10wt%, Na2O content is 8~35wt%;It is stirring Mix it is lower solution A and water glass solution are added sequentially in deionized water, after mixing evenly, the static ageing at 15~50 DEG C Directed agents are made in 0.5~60h;The molar ratio of each component is Na in directed agents2O:Al2O3:SiO2:H2O=15~17:1:15~ 17:300~350;
(2) preparation of slurries D:
According to SAPO-34 molecular sieve: ZSM-11 molecular sieve: aqueous solution mass ratio is 1:0.5~1:3~7, by SAPO-34 and ZSM-11 molecular sieve disperses in aqueous solution, to be heated to 70~80 DEG C, and constant temperature stirs 2~5h, obtains SAPO-34 and ZSM-11 points Sub- screening the pulp liquid adjusts the pH value of SAPO-34 and ZSM-11 molecular sieve pulp, obtains SAPO-34 and ZSM-11 molecular sieve pulp D;
The aqueous solution is the aqueous solution of 1~10wt% potassium hydroxide and 1~5wt% boric acid;
(3) preparation of Y/SAPO-34/ZSM-11 composite molecular screen slurries E:
Silicon source is dissolved in water, Al is formed2O3Content is the solution B of 1~4wt%;
Sodium hydroxide is added to the water with silicon source or aluminium hydroxide is added to the water to after being completely dissolved and adds silicon source, Form sodium aluminate solution C, Al in solution C2O3Content be 3~9wt%, Na2O content is 1~20wt%;
The directed agents, solution B, solution C and slurries D are added to the reaction that synthesis NaY molecular sieve is made in water glass solution Mixture;By the weight of reaction mixture for 100wt% in terms of, the additional amounts of directed agents is 0.5~20wt%, obtains synthesis NaY Reaction mixture each component molar ratio are as follows: Na2O:Al2O3:SiO2:H2O=4~8:1:10~15:200~300;
After reaction mixture crystallization, Y/SAPO-34/ZSM-11 composite molecular screen slurries E is obtained;
(4) preparation of Y/SAPO-34/ZSM-11/ASA multilevel hole material
Surfactant is added in the Y/SAPO-34/ZSM-11 composite molecular screen slurries E, alkaline silicon source or alkali are added Property silicon source solution, and it is adjusted with acid the pH value of system, finally obtained solid mixture matter is filtered, washed, dry, is roasted, Obtain Y/SAPO-34/ZSM-11/ASA multilevel hole material.
2. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (4), the surfactant is at least one of CTAB, P123 and F127.
3. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (4), the additional amount of the surfactant be account for Y/SAPO-34/ZSM-11/ASA multilevel hole material weight 1~ 3wt%.
4. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (2), the pH value is 7~8.
5. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (4), the pH value is 7~9.
6. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (3), the condition of crystallization are as follows: 8~48h of crystallization at 80~140 DEG C.
7. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (1) and (3), source of aluminium is sodium metaaluminate, boehmite, boehmite, aluminum nitrate, aluminum sulfate, aluminium hydroxide One or more of with gibbsite.
8. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (4), it is described alkalinity silicon source be sodium metaaluminate, or be dissolved in sodium hydroxide solution boehmite, boehmite, Aluminium hydroxide or gibbsite.
9. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, it is characterised in that: In step (4), the acid is sulfuric acid, hydrochloric acid or nitric acid.
10. the preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material according to claim 1, feature exist In: mesoporous mesoporous for rule in the Y/SAPO-34/ZSM-11/ASA multilevel hole material, total pore volume is 0.52~0.62mL/ G, Micropore volume are 0.20~0.30mL/g, mesoporous 0.27~0.40mL/g of Kong Rongwei.
CN201710519563.5A 2017-06-29 2017-06-29 Preparation method of Y/SAPO-34/ZSM-11/ASA hierarchical pore material Active CN109205636B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710519563.5A CN109205636B (en) 2017-06-29 2017-06-29 Preparation method of Y/SAPO-34/ZSM-11/ASA hierarchical pore material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710519563.5A CN109205636B (en) 2017-06-29 2017-06-29 Preparation method of Y/SAPO-34/ZSM-11/ASA hierarchical pore material

Publications (2)

Publication Number Publication Date
CN109205636A true CN109205636A (en) 2019-01-15
CN109205636B CN109205636B (en) 2020-02-14

Family

ID=64960895

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710519563.5A Active CN109205636B (en) 2017-06-29 2017-06-29 Preparation method of Y/SAPO-34/ZSM-11/ASA hierarchical pore material

Country Status (1)

Country Link
CN (1) CN109205636B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110368803A (en) * 2019-07-22 2019-10-25 煤科集团沈阳研究院有限公司 A kind of gas absorbent and its preparation method and application
CN110642264A (en) * 2019-11-11 2020-01-03 湘潭大学 Synthesis method of nano needle-shaped ZSM-11 and mixed crystal molecular sieve thereof
CN114195165A (en) * 2020-09-17 2022-03-18 中国石油天然气股份有限公司 Composite carrier with step pore structure distribution and preparation method thereof

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004007647A1 (en) * 2002-07-12 2004-01-22 Shell Internationale Research Maatschappij B.V. Process to prepare a heavy and a light lubricating base oil
CN101205172A (en) * 2006-12-22 2008-06-25 中国石油化工股份有限公司 Method for producing dimethyl ether by fluidized catalytic gas-phase dehydration of methanol
CN101269343A (en) * 2007-03-23 2008-09-24 中国石油天然气股份有限公司 Composite mesoporous molecular sieve hydrocracking catalyst and uses thereof
CN101632938A (en) * 2008-07-24 2010-01-27 中国石油天然气股份有限公司 Middle fraction oil type hydrocracking catalyst
WO2010102430A1 (en) * 2009-03-10 2010-09-16 中国石油天然气股份有限公司 Preparation method for increasing solid content of fcc catalyst
WO2011047527A1 (en) * 2009-10-22 2011-04-28 中国石油天然气股份有限公司 Double micro-mesoporous composite molecular sieve and preparation method thereof
WO2011047528A1 (en) * 2009-10-22 2011-04-28 中国石油天然气股份有限公司 Bi-microporous-mesoporous composite molecular sieve y-beta/ mcm-41 and preparing method thereof
CN102533316A (en) * 2010-12-23 2012-07-04 中国石油天然气股份有限公司 Method for selective hydrocracking of light oil
CN102553638A (en) * 2010-12-17 2012-07-11 中国石油天然气股份有限公司 Double-microporous-mesoporous composite molecular sieve hydrocracking catalyst
CN102553637A (en) * 2010-12-17 2012-07-11 中国石油天然气股份有限公司 Medium oil hydrocracking catalyst carrier and preparation and application thereof
CN103896299A (en) * 2012-12-27 2014-07-02 中国石油天然气股份有限公司 Method for synthesizing SAPO-31 molecular sieve nanocrystal from double templates
CN104707646A (en) * 2013-12-11 2015-06-17 中国科学院青岛生物能源与过程研究所 Catalyst for toluene preparation through oxidative dehydrogenation of dimethyl ether, preparation method and applications thereof
US20170114157A1 (en) * 2015-10-21 2017-04-27 Saudi Arabian Oil Company Cationic polymers and porous materials

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004007647A1 (en) * 2002-07-12 2004-01-22 Shell Internationale Research Maatschappij B.V. Process to prepare a heavy and a light lubricating base oil
CN101205172A (en) * 2006-12-22 2008-06-25 中国石油化工股份有限公司 Method for producing dimethyl ether by fluidized catalytic gas-phase dehydration of methanol
CN101269343A (en) * 2007-03-23 2008-09-24 中国石油天然气股份有限公司 Composite mesoporous molecular sieve hydrocracking catalyst and uses thereof
CN101632938A (en) * 2008-07-24 2010-01-27 中国石油天然气股份有限公司 Middle fraction oil type hydrocracking catalyst
WO2010102430A1 (en) * 2009-03-10 2010-09-16 中国石油天然气股份有限公司 Preparation method for increasing solid content of fcc catalyst
WO2011047528A1 (en) * 2009-10-22 2011-04-28 中国石油天然气股份有限公司 Bi-microporous-mesoporous composite molecular sieve y-beta/ mcm-41 and preparing method thereof
WO2011047527A1 (en) * 2009-10-22 2011-04-28 中国石油天然气股份有限公司 Double micro-mesoporous composite molecular sieve and preparation method thereof
CN102553638A (en) * 2010-12-17 2012-07-11 中国石油天然气股份有限公司 Double-microporous-mesoporous composite molecular sieve hydrocracking catalyst
CN102553637A (en) * 2010-12-17 2012-07-11 中国石油天然气股份有限公司 Medium oil hydrocracking catalyst carrier and preparation and application thereof
CN102533316A (en) * 2010-12-23 2012-07-04 中国石油天然气股份有限公司 Method for selective hydrocracking of light oil
CN103896299A (en) * 2012-12-27 2014-07-02 中国石油天然气股份有限公司 Method for synthesizing SAPO-31 molecular sieve nanocrystal from double templates
CN104707646A (en) * 2013-12-11 2015-06-17 中国科学院青岛生物能源与过程研究所 Catalyst for toluene preparation through oxidative dehydrogenation of dimethyl ether, preparation method and applications thereof
US20170114157A1 (en) * 2015-10-21 2017-04-27 Saudi Arabian Oil Company Cationic polymers and porous materials

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110368803A (en) * 2019-07-22 2019-10-25 煤科集团沈阳研究院有限公司 A kind of gas absorbent and its preparation method and application
CN110368803B (en) * 2019-07-22 2021-10-22 煤科集团沈阳研究院有限公司 Gas absorbent and preparation method and application thereof
CN110642264A (en) * 2019-11-11 2020-01-03 湘潭大学 Synthesis method of nano needle-shaped ZSM-11 and mixed crystal molecular sieve thereof
CN110642264B (en) * 2019-11-11 2020-12-29 湘潭大学 Synthesis method of nano needle-shaped ZSM-11 and mixed crystal molecular sieve thereof
CN114195165A (en) * 2020-09-17 2022-03-18 中国石油天然气股份有限公司 Composite carrier with step pore structure distribution and preparation method thereof
CN114195165B (en) * 2020-09-17 2023-08-22 中国石油天然气股份有限公司 Composite carrier with step hole structure distribution and preparation method thereof

Also Published As

Publication number Publication date
CN109205636B (en) 2020-02-14

Similar Documents

Publication Publication Date Title
CN107519933B (en) Y/EU-1/SBA-15/ASA/MOF composite material and preparation method
CN101759198B (en) Small crystal particle Y-shaped molecular sieve and preparation method thereof
CN104591214B (en) A kind of small crystal grain Y-shaped molecular sieve and preparation method thereof
CN109205636A (en) The preparation method of Y/SAPO-34/ZSM-11/ASA multilevel hole material
CN105621449B (en) A kind of NaY types molecular sieve and preparation method thereof
CN102616807B (en) Method for synthesizing Y type molecular sieve
CN109304226A (en) A kind of hydrocracking catalyst and its preparation method and application of fecund heavy naphtha and boat coal
CN107344721B (en) A kind of Modified Zeolite Y and its preparation method and application
CN106946268B (en) A kind of MOR/ZSM-35 composite molecular screen and its synthetic method
CN107519927B (en) Y/ZSM-22/SAPO-34/ASA/MOF composite material and preparation method
JP5555192B2 (en) Novel pentasil-type zeolite and synthesis method thereof
CN107519923B (en) Y/EU-1/ZSM-5/ASA/ heteropoly acid composite material and preparation method
CN106946267B (en) A kind of EU-1 molecular sieve and its synthetic method
CN104549459A (en) Composite molecular sieve, as well as synthesis method and application thereof
CN105084388B (en) Method for preparing and modifying Y-type molecular sieve
CN107519922B (en) Y/Gd2O3/ ZSM-23/ZSM-5/ASA composite material and preparation method
CN107519921B (en) Y/Sm2O3/ ZSM-22/ZSM-5/ASA composite material and preparation method
CN107519938B (en) Y/CeO2/ SBA-15/ASA/MOF composite material and preparation method
CN107519924B (en) Y/EU-1/ZSM-23/ZSM-5/ASA composite material and preparation method
CN107519925B (en) Y/Sm2O3/ SBA-3/ASA composite material and preparation method
CN101417810A (en) Mesoporous material and preparation method thereof
CN112808296B (en) Catalyst containing Y-type molecular sieve and preparation method thereof
CN101830479B (en) Fluorine-contained T-shaped zeolite molecular sieve and preparation method thereof
CN109422274A (en) A kind of preparation method of multilevel hole material
CN106946269B (en) A kind of MCM-22/MOR composite molecular screen and its synthetic method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant