CN106809862A - A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves - Google Patents

A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves Download PDF

Info

Publication number
CN106809862A
CN106809862A CN201510855771.3A CN201510855771A CN106809862A CN 106809862 A CN106809862 A CN 106809862A CN 201510855771 A CN201510855771 A CN 201510855771A CN 106809862 A CN106809862 A CN 106809862A
Authority
CN
China
Prior art keywords
stage porous
molecular sieves
crystallization
silicon source
sapo
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.)
Pending
Application number
CN201510855771.3A
Other languages
Chinese (zh)
Inventor
田志坚
陶硕
厉晓蕾
徐仁顺
马怀军
王炳春
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.)
Dalian Institute of Chemical Physics of CAS
Original Assignee
Dalian Institute of Chemical Physics of CAS
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 Dalian Institute of Chemical Physics of CAS filed Critical Dalian Institute of Chemical Physics of CAS
Priority to CN201510855771.3A priority Critical patent/CN106809862A/en
Publication of CN106809862A publication Critical patent/CN106809862A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • 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
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2002/00Crystal-structural characteristics
    • C01P2002/70Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
    • C01P2002/72Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/01Particle morphology depicted by an image
    • C01P2004/03Particle morphology depicted by an image obtained by SEM
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/16Pore diameter
    • C01P2006/17Pore diameter distribution

Abstract

The invention discloses a kind of method and its molecular sieve for preparing multi-stage porous SAPO-11.It is aided in or Vapor-phase transport method using vapor, with mesoporous SAPO gel as presoma, synthesis obtains a kind of multi-stage porous SAPO-11 molecular sieves that the AEL structure that association (International Zeolite Association) confirms is sieved with International Molecular.Multi-stage porous SAPO-11 molecular sieves of the invention have good hydrothermal stability, there is big specific surface area and pore volume simultaneously, to be with a wide range of applications in catalytic field particularly lube base oil hydroisomerizing field, preparation method economy of the present invention is strong, easy-to-operate, it is environment-friendly.

Description

A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves
Technical field
The present invention relates to a kind of synthetic method of silicoaluminophosphamolecular molecular sieves in high yield, more precisely close In a kind of synthetic method for preparing multi-stage porous SAPO-11 molecular sieves in high yield.
Background technology
SAPO-11 is the silicoaluminophosphamolecular molecular sieves with AEL (International Zeolite Association's appointment codes) structure (Atlas of Zeolite Framework Types,6thed.,Elsevier,Amsterdam,2007;http:// Www.iza-structure.org/databases/) it has one-dimensional oval 10 yuan of rings straight hole road, aperture size It is 0.40nm × 0.65nm.Because the pore passage structure size of this molecular sieve is highly beneficial with geometric configuration In the formation of single branched paraffin isomers, the Pt-Pd/AEL silicoaluminophosphamolecular molecular sieves of Supported Pt Nanoparticles palladium noble metal Good catalysis activity and selectivity is shown in the isomerization reaction of linear paraffin.But itself The micropore being had is unfavorable for the diffusion of molecule, limits its catalysis activity.Therefore, researcher is using each Method is planted to attempt to introduce mesoporous or macropore.(J.Catal.2012,294,161-170;J.Catal.2013,301, 162-173).The common feature of these methods is that the surfactant that costliness is added under conditions of hydro-thermal is closed Into.Zeolite synthesis yield is low, complex process, operating difficulties;Surfactant is expensive, no Can reclaim, synthesize high cost.
Xerogel synthesis includes vapor auxiliary law and Vapor-phase transport method, and the method is by China scientist Xu Wen Yang teach method that proposed in nineteen ninety a kind of new prepare molecular sieve (J.Chem.Soc., Chem.Commun.1990,(10),755).The method is typically unformed raw material and water, You Jimo Unformed gel is prepared into after plate agent is well mixed, precursor mixture is obtained after drying.Precursor is mixed During thing is as special container, a small amount of water is added in a kettle., to provide the moisture required for reaction, Then crystallization under steam ambient again.Compared to traditional Hydrothermal Synthesiss, xerogel synthesis has high income, It is low in the pollution of the environment, the features such as raw material availability is high.
Although report prepare the SAPO-11 molecules with AEL skeletons using vapor auxiliary law before The preparation of sieve, due to the crystal it typically is needle-like, single micropore limits its answering in terms of catalysis With.The sol-gal process that this patent employs epoxide participation is prepared with bigger serface, The mesoporous SAPO gel precursors mixture of big pore volume, the precursor mixture is aided in vapor Under the conditions of synthesized AEL type multi-stage porous SAPO-11 molecular sieves, because it has in high yield and simultaneously With micropore and mesoporous, will especially lube base oil hydroisomerizing field obtains more in catalytic field Good application.
The content of the invention
It is an object of the invention to propose a kind of method for preparing multi-stage porous SAPO-11 molecular sieves in high yield.
To achieve the above object, the technical solution adopted by the present invention is:
It is auxiliary in vapor with organic amine as template with mesoporous SAPO gel as precursor mixture By the synthesis of SAPO gel with multi-stage porous SAPO-11 molecular sieves in high yield under conditions of helping;Bag Include following steps:
1) preparation of precursor mixture:Add phosphorus source, silicon source and silicon source in solvent, stirring is to equal Epoxide is added after even, after continuing to be stirred until homogeneous, it is aging at a certain temperature and dry before Drive body mixture;
2) precursor mixture is placed in container, and is placed in crystallization system, in crystallization system Bottom adds water and has organic amine;
3) heating crystallization, after crystallization terminates, separates solid product, and the solid for obtaining is multi-stage porous SAPO-11 Molecular sieve.
Concretely comprise the following steps:
During phosphorus source added into solvent, and stir;Silicon source is added in mixture, is stirred; Silicon source is added, is stirred;To above-mentioned solution in ethylene compound, stir;By above-mentioned mixing Thing is aging in 0~200 DEG C, and the aging temperature of optimization is 10~60 DEG C;Mixture after will be aging is dried, Drying temperature is 40~200 DEG C, and the drying temperature of optimization is 60~120 DEG C, and precursor mixing is obtained after drying Thing.By precursor mixture in the presence of organic amine, vapor auxiliary crystallization, crystallization temperature be 100~ 200 DEG C, crystallization time is more than or equal to 1 minute, and preferred crystallization time is 0.5~480h;
Crystallization separates solid product after terminating, will reactant mixture be cooled to room temperature, plus deionized water, Filtering, is washed, room temperature~120 DEG C drying with deionized water to sample, and the solid sample for obtaining is With multi-stage porous SAPO-11 molecular sieves in high yield;
Roasting (300~600 DEG C of air atmosphere roastings are more than or equal to 1 hour) removes organic formwork afterwards Agent, obtains the multi-stage porous silicoaluminophosphamolecular molecular sieves of duct dredging, and the duct dredging is molecular sieve pore passage In be free of organic formwork agent.
Step 1) silicon source in precursor mixture:Silicon source:Phosphorus source:Epoxide:Solvent presses Al2O3: SiO2:P2O5:Epoxide:The molar ratio of solvent meter is 1:0.01~1:0.1~5:0.01~ 50:5~200, aging temperature is 0~200 DEG C, and drying temperature is 40~200 DEG C;Step 2) precursor Mixture:Water:The molar ratio of organic amine is 1:0.01~1000:0.1~50, wherein precursor mixing The mole of thing is with the molar amount of phosphorus source;Step 3) crystallization temperature be 80 DEG C~300 DEG C, during crystallization Between be more than or equal to 1 minute.
Step 1) silicon source in precursor mixture:Silicon source:Phosphorus source:Epoxide:Solvent presses Al2O3: SiO2:P2O5:Epoxide:The mol ratio of solvent meter is 1:0.1~0.8:0.5~3:0.5~20: 10~50, aging temperature is 10~60 DEG C, and drying temperature is 60~120 DEG C;Step 2) precursor mixing Thing:Water:The molar ratio of organic amine is 1:0.1~100:0.5~30, wherein precursor mixture rubs You are measured with the molar amount of phosphorus source;Step 3) crystallization temperature be 120~240 DEG C, crystallization time be 1~ 240h。
Solvent be water, ethanol, propyl alcohol, isopropanol and ethylene glycol in one or more;Phosphorus source It is one or two or more kinds in phosphoric acid, ammonium phosphate, monoammonium phosphate and ammonium dihydrogen phosphate, the phosphorus Sour mass concentration is 50-85%;Silicon source is aluminium isopropoxide, crystal aluminum chloride, boehmite, sulfuric acid One or two or more kinds in aluminium;During silicon was Ludox, waterglass, white carbon, tetraethyl orthosilicate originally One or two or more kinds;Epoxide be oxirane and expoxy propane in one or two; Organic amine is one kind or two kinds in dimethylamine, diethylamine, di-n-propylamine, diisopropylamine, n-butylamine More than.
Crystallization system is stainless steel cauldron or microwave reactor.
Product has the characteristics of in high yield, and product yield is 40~100%.
After the fired removal organic formwork agent of prepared molecular sieve, the multistage of duct dredging can be obtained Hole silicoaluminophosphamolecular molecular sieves, the duct dredging is to be free of organic formwork agent in molecular sieve pore passage, roasting is warm It is 300~600 DEG C to spend, and roasting time is more than or equal to 1 hour.
Molecular sieve prepared by the preparation method provided according to the present invention uses X-ray powder diffraction, X to penetrate Line spectrofluorimetry and SEM (SEM) are analyzed to the molecular sieve structure and composition, Determine that its structure is true with International Molecular sieve association by comparing with XRD powder diffraction datas storehouse card The AEL structure recognized, X-ray fluorescence spectra constituent content analysis result determines Al in the molecular sieve2O3: P2O5:SiO2Molar ratio, is characterized by SEM and determines its pattern.The molecular sieve for finally giving has state The AEL structure that border molecular sieve association confirms, while silicon source in the molecular sieve:Silicon source:Phosphorus source presses Al2O3: SiO2:P2O5Meter, molar ratio is 1:0.1~0.6:0.8~1.2.Its X-ray diffraction spectrogram is extremely There is diffraction maximum set forth below less,
2 θ values expression diffraction maximum position, 2 θ/°:8.10±0.2,9.51±0.2,13.18± 0.2,13.65±0.2,15.71±0.2,16.23±0.2,19.03±0.2,20.38±0.2,21.08 ±0.2,22.12±0.2,22.79±0.2,23.17±0.2,24.77±0.2,26.33± 0.2,28.70±0.2,29.50±0.2。
The beneficial effect of this synthetic method:
The characteristics of this synthetic method is to carry out multi-stage porous SAPO-11 molecules under conditions of vapor auxiliary The synthesis of sieve, overcomes the characteristics of conventional hydrothermal synthetic product yield is low, and waste discharge is serious.Closed Into material be the multi-stage porous SAPO-11 molecular sieves with AEL structure.The inventive method has environment Close friend, easy to operate, the advantage of high income,.
Brief description of the drawings
Fig. 1 is the XRD spectra of the multi-stage porous SAPO-11 molecular sieves synthesized by the embodiment of the present invention 1.
Fig. 2 is that the nitrogen physisorption of the multi-stage porous SAPO-11 molecular sieves synthesized by the embodiment of the present invention 1 is inhaled Attached curve.
Fig. 3 is the SEM Electronic Speculum of the multi-stage porous SAPO-11 molecular sieves synthesized by the embodiment of the present invention 1 Photo.
Specific embodiment
Embodiment 1
To 10 grams of water are added in 50 milliliters of beakers, 2.0g crystal aluminum chlorides are added under magnetic agitation, It is even that the phosphoric acid that 1.5 gram mass concentration are 85% is added dropwise, 0.3 gram of tetraethyl orthosilicate is added dropwise after stirring, Stirring 30 minutes, is then dropwise added dropwise 2 milliliters of expoxy propane, continues to stir 5 minutes.By mixture In aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Above-mentioned precursor is taken to mix During 1 gram of compound is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, The bottom of reactor adds 1 gram of water, 0.5 gram of positive di-n-propylamine that 200 DEG C are warming up to after sealing, 2 are kept My god, reactant mixture is then cooled to room temperature, and be washed with deionized 3 times.By final white Powder is placed in 120 DEG C of baking ovens and dries, and is tested through XRD, SEM, and the white powder is with AEL knots The multi-stage porous silicoaluminophosphamolecular molecular sieves of structure.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains To the multi-stage porous SAPO-11 molecular sieves that duct is dredged.
Embodiment 2
To 5 grams of water, 5 grams of ethanol are added in 50 milliliters of beakers, 2.0g crystallization chlorinations are added under magnetic agitation Aluminium, it is uniform that the phosphoric acid that 1.5 gram mass concentration are 85% is added dropwise, 0.5 gram of positive silicic acid is added dropwise after stirring Ethyl ester, stirs 30 minutes, and 2 milliliters of expoxy propane are then dropwise added dropwise, and continues to stir 5 minutes.Will Mixture in aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Take above-mentioned During 1 gram of precursor mixture is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron In, add 1 gram of water, 1 gram of positive di-n-propylamine 200 DEG C to be warming up to after sealing, is protected in the bottom of reactor Hold 2 days, reactant mixture is then cooled to room temperature, and be washed with deionized 3 times.Will be final White powder is placed in 120 DEG C of baking ovens and dries, and is tested through XRD, SEM, and the white powder is with AEL The multi-stage porous silicoaluminophosphamolecular molecular sieves of structure.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, Obtain the multi-stage porous SAPO-11 molecular sieves of duct dredging.
Embodiment 3
To 10 ethanol are added in 50 milliliters of beakers, 2.0g crystal aluminum chlorides are added under magnetic agitation, It is even that the phosphoric acid that 1.5 gram mass concentration are 85% is added dropwise, 0.4 gram of tetraethyl orthosilicate is added dropwise after stirring, Stirring 30 minutes, is then dropwise added dropwise 3 milliliters of expoxy propane, continues to stir 5 minutes.By mixture In aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Above-mentioned precursor is taken to mix During 1 gram of compound is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, The bottom of reactor adds 1 gram of water, 0.5 gram of positive di-n-propylamine that 200 DEG C are warming up to after sealing, 2 are kept My god, reactant mixture is then cooled to room temperature, and be washed with deionized 3 times.By final white Powder is placed in 120 DEG C of baking ovens and dries, and is tested through XRD, SEM, and the white powder is with AEL knots The multi-stage porous silicoaluminophosphamolecular molecular sieves of structure.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains To the multi-stage porous SAPO-11 molecular sieves that duct is dredged.
Embodiment 4
To 10 grams of water are added in 50 milliliters of beakers, 2.0g crystal aluminum chlorides are added under magnetic agitation, uniformly The phosphoric acid that 2.0 gram mass concentration are 85% is added dropwise, 0.3 gram of tetraethyl orthosilicate is added dropwise after stirring, stir Mix 30 minutes, 4 milliliters of expoxy propane are then dropwise added dropwise, continue to stir 5 minutes.By mixture in Aging 12 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Take above-mentioned precursor mixing During 1 gram of thing is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, anti- The bottom of kettle is answered to add 1 gram of water, 0.5 gram of positive di-n-propylamine 200 DEG C to be warming up to after sealing, is kept for 2 days, Then reactant mixture is cooled to room temperature, and is washed with deionized 3 times.By final white powder It is placed in 120 DEG C of baking ovens and dries, tested through XRD, SEM, the white powder is with AEL structure Multi-stage porous silicoaluminophosphamolecular molecular sieves.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains hole The multi-stage porous SAPO-11 molecular sieves of road dredging.
Embodiment 5
To 10 grams of water are added in 50 milliliters of beakers, 2.00g crystal aluminum chlorides are added under magnetic agitation, It is even that the phosphoric acid that 1.5 gram mass concentration are 85% is added dropwise, 0.6 gram of tetraethyl orthosilicate is added dropwise after stirring, Stirring 30 minutes, is then dropwise added dropwise 5 milliliters of expoxy propane, continues to stir 5 minutes.By mixture In aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Above-mentioned precursor is taken to mix During 1 gram of compound is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, The bottom of reactor adds 1 gram of water, 0.6 gram of positive di-n-propylamine that 200 DEG C are warming up to after sealing, 2 are kept My god, reactant mixture is then cooled to room temperature, and be washed with deionized 3 times.By final white Powder is placed in 120 DEG C of baking ovens and dries, and is tested through XRD, SEM, and the white powder is with AEL knots The multi-stage porous silicoaluminophosphamolecular molecular sieves of structure.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains To the multi-stage porous SAPO-11 molecular sieves that duct is dredged.
Embodiment 6
To 10 grams of ethanol are added in 50 milliliters of beakers, 2.00g crystal aluminum chlorides are added under magnetic agitation, It is uniform that the phosphoric acid that 1.2 gram mass concentration are 85% is added dropwise, 0.4 gram of tetraethyl orthosilicate is added dropwise after stirring, Stirring 30 minutes, is then dropwise added dropwise 2 milliliters of expoxy propane, continues to stir 5 minutes.By mixture In aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Above-mentioned precursor is taken to mix During 1 gram of compound is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, The bottom of reactor adds 1 gram of water, 0.5 gram of positive di-n-propylamine that 200 DEG C are warming up to after sealing, 2 are kept My god, reactant mixture is then cooled to room temperature, and be washed with deionized 3 times.By final white Powder is placed in 120 DEG C of baking ovens and dries, and is tested through XRD, SEM, and the white powder is with AEL knots The multi-stage porous silicoaluminophosphamolecular molecular sieves of structure.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains To the multi-stage porous SAPO-11 molecular sieves that duct is dredged.Embodiment 9
Embodiment 7
To 10 grams of water are added in 50 milliliters of beakers, 2.00g crystal aluminum chlorides are added under magnetic agitation, uniformly The phosphoric acid that 1.8 gram mass concentration are 85% is added dropwise, 0.3 gram of tetraethyl orthosilicate is added dropwise after stirring, stir Mix 30 minutes, 4 milliliters of expoxy propane are then dropwise added dropwise, continue to stir 5 minutes.By mixture in Aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 120 degree.Take above-mentioned precursor mixing During 1 gram of thing is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, anti- The bottom of kettle is answered to add 1 gram of water, 0.5 gram of positive di-n-propylamine 200 DEG C to be warming up to after sealing, is kept for 2 days, Then reactant mixture is cooled to room temperature, and is washed with deionized 3 times.By final white powder It is placed in 120 DEG C of baking ovens and dries, tested through XRD, SEM, the white powder is with AEL structure Multi-stage porous silicoaluminophosphamolecular molecular sieves.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains hole The multi-stage porous SAPO-11 molecular sieves of road dredging.Embodiment 11
Embodiment 8
To 10 grams of water are added in 50 milliliters of beakers, 2.00g crystal aluminum chlorides are added under magnetic agitation, It is even that the phosphoric acid that 1.5 gram mass concentration are 85% is added dropwise, 0.3 gram of tetraethyl orthosilicate is added dropwise after stirring, Stirring 30 minutes, is then dropwise added dropwise 2 milliliters of expoxy propane, continues to stir 5 minutes.By mixture In aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Above-mentioned precursor is taken to mix During 1 gram of compound is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, The bottom of reactor adds 0.5 gram of water, 0.5 gram of positive di-n-propylamine that 180 DEG C are warming up to after sealing, 2 are kept My god, reactant mixture is then cooled to room temperature, and be washed with deionized 3 times.By final white Powder is placed in 120 DEG C of baking ovens and dries, and is tested through XRD, SEM, and the white powder is with AEL knots The multi-stage porous silicoaluminophosphamolecular molecular sieves of structure.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains To the multi-stage porous SAPO-11 molecular sieves that duct is dredged.
Embodiment 9
To 10 grams of water are added in 50 milliliters of beakers, 2.00g crystal aluminum chlorides are added under magnetic agitation, uniformly The phosphoric acid that 1.2 gram mass concentration are 85% is added dropwise, 0.2 gram of tetraethyl orthosilicate is added dropwise after stirring, stir Mix 30 minutes, 5 milliliters of expoxy propane are then dropwise added dropwise, continue to stir 5 minutes.By mixture in Aging 24 hours at 40 DEG C, then in drying to obtain precursor mixture under 100 degree.Take above-mentioned precursor mixing During 1 gram of thing is placed in standoff tetrafluoro pallet, and by pallet as stainless steel cauldron in, anti- The bottom of kettle is answered to add 1.5 grams of water, 0.5 gram of positive di-n-propylamine that 200 DEG C are warming up to after sealing, 2 are kept My god, reactant mixture is then cooled to room temperature, and be washed with deionized 3 times.By final white Powder is placed in 120 DEG C of baking ovens and dries, and is tested through XRD, SEM, and the white powder is with AEL knots The multi-stage porous silicoaluminophosphamolecular molecular sieves of structure.Products therefrom is calcined 24h through 570 DEG C under air atmosphere, obtains To the multi-stage porous SAPO-11 molecular sieves that duct is dredged.

Claims (9)

1. a kind of method for preparing multi-stage porous SAPO-11 molecular sieves, it is characterised in that:With mesoporous phosphoric acid Silica-alumina gel is presoma, with organic amine as template, by silicon phosphate under conditions of vapor auxiliary Alumina gel synthesizes multi-stage porous SAPO-11 molecular sieves;Comprise the following steps:
1) preparation of precursor mixture:Phosphorus source, silicon source and silicon source are added in solvent, is stirred until homogeneous After add epoxide, after continuing to be stirred until homogeneous, aging at a certain temperature and dry forerunner Body mixture;
2) precursor mixture is placed in container, and is placed in crystallization system, in crystallization system Bottom adds water and has organic amine;
3) heating crystallization, after crystallization terminates, separates solid product, and the solid for obtaining is multi-stage porous SAPO-11 Molecular sieve.
2. in accordance with the method for claim 1, it is characterised in that:Step 1) in precursor mixture Silicon source:Silicon source:Phosphorus source:Epoxide:Solvent presses Al2O3:SiO2:P2O5:Epoxide: The molar ratio of solvent meter is 1:0.01~1:0.1~5:0.01~50:5~200, aging temperature is 0~200 DEG C, drying temperature is 40~200 DEG C;Step 2) precursor mixture:Water:Organic amine rubs Your ratio is 1:0.01~1000:0.1~50, wherein the mole of precursor mixture with phosphorus source mole Gauge;Step 3) crystallization temperature be 80 DEG C~300 DEG C, crystallization time be more than or equal to 1 minute.
3. according to the method described in claim 1 or 2, it is characterised in that:Step 1) precursor mixing Silicon source in thing:Silicon source:Phosphorus source:Epoxide:Solvent presses Al2O3:SiO2:P2O5:Epoxy compound Thing:The mol ratio of solvent meter is 1:0.1~0.8:0.5~3:0.5~20:10~50, aging temperature It it is 10~60 DEG C, drying temperature is 60~120 DEG C;Step 2) precursor mixture:Water:Organic amine Molar ratio is 1:0.1~100:0.5~30, wherein the mole of precursor mixture with phosphorus source mole Gauge;Step 3) crystallization temperature be 120~240 DEG C, crystallization time be 1~240h.
4. in accordance with the method for claim 1, it is characterised in that:Solvent be water, ethanol, propyl alcohol, One or more in isopropanol and ethylene glycol;Phosphorus source is phosphoric acid, ammonium phosphate, monoammonium phosphate With one or two or more kinds in ammonium dihydrogen phosphate, the phosphoric acid quality concentration is 50-85%;Silicon source is One or two or more kinds in aluminium isopropoxide, crystal aluminum chloride, boehmite, aluminum sulfate;Silicon is former It is one or two or more kinds in Ludox, waterglass, white carbon, tetraethyl orthosilicate;Epoxy compound Thing be oxirane and expoxy propane in one or two;Organic amine is dimethylamine, diethylamine, two One or two or more kinds in n-propylamine, diisopropylamine, n-butylamine.
5. in accordance with the method for claim 1, it is characterised in that:Crystallization system is stainless steel reaction Kettle or microwave reactor.
6. in accordance with the method for claim 1, it is characterised in that:Product has the characteristics of in high yield, Product yield is 40~100%.
7. in accordance with the method for claim 1, it is characterised in that:Prepared molecular sieve is fired After removal organic formwork agent, the multi-stage porous silicoaluminophosphamolecular molecular sieves of duct dredging, the duct can be obtained Dredge to be free of organic formwork agent in molecular sieve pore passage.
8. in accordance with the method for claim 7, it is characterised in that:Sintering temperature is 300~600 DEG C, Roasting time is more than or equal to 1 hour.
9. the molecular sieve that prepared by any preparation method described in usage right requirement 1~7, it is characterised in that: There is multi-stage porous SAPO-11 molecular sieves International Molecular to sieve the AEL structure that association confirms, while the molecule Silicon source in sieve:Silicon source:Phosphorus source presses Al2O3:SiO2:P2O5Meter, molar ratio is 1:0.1~0.6:0.8~ 1.2;Its X-ray diffraction spectrogram at least has diffraction maximum set forth below,
2 θ values expression diffraction maximum position, 2 θ/°:8.10±0.2,9.51±0.2,13.18± 0.2,13.65±0.2,15.71±0.2,16.23±0.2,19.03±0.2,20.38±0.2,21.08 ±0.2,22.12±0.2,22.79±0.2,23.17±0.2,24.77±0.2,26.33± 0.2,28.70±0.2,29.50±0.2。
CN201510855771.3A 2015-11-27 2015-11-27 A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves Pending CN106809862A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510855771.3A CN106809862A (en) 2015-11-27 2015-11-27 A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510855771.3A CN106809862A (en) 2015-11-27 2015-11-27 A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves

Publications (1)

Publication Number Publication Date
CN106809862A true CN106809862A (en) 2017-06-09

Family

ID=59157148

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510855771.3A Pending CN106809862A (en) 2015-11-27 2015-11-27 A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves

Country Status (1)

Country Link
CN (1) CN106809862A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109896531A (en) * 2019-04-21 2019-06-18 王干 A kind of preparation method of SAPO-11 molecular sieve
CN112456513A (en) * 2020-12-10 2021-03-09 聊城大学 Open system solid phase synthesis AEL structure aluminum phosphate based molecular sieve, preparation method and application
CN114939434A (en) * 2022-06-01 2022-08-26 南京工业大学 Process for catalyzing hydroisomerization of n-hexane

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1834015A (en) * 2005-03-18 2006-09-20 中国科学院大连化学物理研究所 Synthetic process of SAPO-11 Molecular sieve
CN101081700A (en) * 2007-06-11 2007-12-05 大连理工大学 Preparation method of zeolite molecular sieve having ordered meso-porous structure
CN101913622A (en) * 2010-08-25 2010-12-15 中国石油大学(北京) Preparation method of multistage pore canal SAPO-11 (silicoaluminophosphate-11) molecular sieve and application thereof in gasoline modification
CN102219236A (en) * 2010-04-15 2011-10-19 中国石油化工股份有限公司 Multi-stage porous structure SAPO (silicoaluminophosphate) molecular sieve monolith material and preparation method thereof
CN104556092A (en) * 2013-10-28 2015-04-29 中国石油化工股份有限公司 Hierarchical porous structure SAPO molecular sieve material and preparation method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1834015A (en) * 2005-03-18 2006-09-20 中国科学院大连化学物理研究所 Synthetic process of SAPO-11 Molecular sieve
CN101081700A (en) * 2007-06-11 2007-12-05 大连理工大学 Preparation method of zeolite molecular sieve having ordered meso-porous structure
CN102219236A (en) * 2010-04-15 2011-10-19 中国石油化工股份有限公司 Multi-stage porous structure SAPO (silicoaluminophosphate) molecular sieve monolith material and preparation method thereof
CN101913622A (en) * 2010-08-25 2010-12-15 中国石油大学(北京) Preparation method of multistage pore canal SAPO-11 (silicoaluminophosphate-11) molecular sieve and application thereof in gasoline modification
CN104556092A (en) * 2013-10-28 2015-04-29 中国石油化工股份有限公司 Hierarchical porous structure SAPO molecular sieve material and preparation method thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
LIN GUO ET AL.: "Impact of cationic surfactant chain length during SAPO-11 molecular sieve synthesis on structure, acidity, and n-octane isomerization to di-methyl hexanes", 《JOURNAL OF CATALYSIS》 *
LIN GUO ET AL.: "Two-stage surfactant-assisted crystallization for enhancing SAPO-11 acidity to improve n-octane di-branched isomerization", 《JOURNAL OF CATALYSIS》 *
YAN LIU ET AL.: "Catalytically active and hierarchically porous SAPO-11 zeolite synthesized in the presence of polyhexamethylene biguanidine", 《JOURNAL OF COLLOID AND INTERFACE SCIENCE》 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109896531A (en) * 2019-04-21 2019-06-18 王干 A kind of preparation method of SAPO-11 molecular sieve
CN112456513A (en) * 2020-12-10 2021-03-09 聊城大学 Open system solid phase synthesis AEL structure aluminum phosphate based molecular sieve, preparation method and application
CN112456513B (en) * 2020-12-10 2023-05-09 聊城大学 Open system solid phase synthesis AEL structure aluminum phosphate based molecular sieve, preparation method and application
CN114939434A (en) * 2022-06-01 2022-08-26 南京工业大学 Process for catalyzing hydroisomerization of n-hexane

Similar Documents

Publication Publication Date Title
CN106185977B (en) A kind of method of green syt ZSM-5 molecular sieve
Egeblad et al. Mesoporous zeolite and zeotype single crystals synthesized in fluoride media
CN102795635B (en) Multi-orifice zeolite material as well as preparation method and application thereof
CN101683620B (en) Cubic mesoporous molecular sieve catalyst with micropore canals, preparation method and use thereof
CN101935053B (en) ZSM-5 zeolite and synthesis method thereof
JP6383100B2 (en) Method for producing high silica alumina ratio Y-type molecular sieve
CN108557838B (en) Preparation method of silicon-phosphorus-aluminum molecular sieve
Utchariyajit et al. Effect of synthesis parameters on mesoporous SAPO-5 with AFI-type formation via microwave radiation using alumatrane and silatrane precursors
CN108217680B (en) Method for synthesizing mordenite MOR molecular sieve, product and application thereof
WO2018103089A1 (en) Method for synthesizing mordenite mor molecular sieve, and product and use thereof
CN106607081B (en) A kind of method of organic phosphorus compound modified zsm-5 zeolite
CN108128786B (en) A kind of method that ultrasonic wave added prepares multi-stage porous SAPO-11 molecular sieve
CN106809862A (en) A kind of method and its molecular sieve for preparing multi-stage porous SAPO-11 molecular sieves
CN105271303B (en) AEL structure rare earth replaces the preparation method of aluminium phosphate molecular sieve
CN101993092A (en) Method for synthesizing ZSM-5 zeolite
CN106582804A (en) Hierarchical porous SAPO-34/kaolin composite material and preparation method thereof
CN106809861A (en) The preparation method and its molecular sieve of a kind of bigger serface SAPO-11 molecular sieves
CN108285152A (en) A kind of green high-efficient synthetic method of Copper-cladding Aluminum Bar SBA-15 meso-porous molecular sieve materials
CN103466654B (en) Preparation method of ZSM-5 mesoporous and microporous composite molecular sieve
CN106276964B (en) A kind of transgranular phosphorous ZSM-5 molecular sieve and preparation method thereof
CN105753006B (en) A kind of preparation of AEL structure multi-stage porous silicoaluminophosphamolecular molecular sieves and molecular sieve
CN104909382B (en) Method for preparing Beta zeolite molecular sieve with excessive chiral polymorph A under acidic condition
CN109574036B (en) Preparation method of DNL-1 molecular sieve
CN106517229B (en) The method that hydrothermal synthesis method prepares nano-sheet SAPO-11 molecular sieves
CN109319806A (en) A kind of method of the integral formula SSZ-13 molecular sieve of mixed templates dry glue

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
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20170609