CN107954438A - Lead directly to mesoporous FAU molecular sieves and preparation method thereof - Google Patents

Lead directly to mesoporous FAU molecular sieves and preparation method thereof Download PDF

Info

Publication number
CN107954438A
CN107954438A CN201610899052.6A CN201610899052A CN107954438A CN 107954438 A CN107954438 A CN 107954438A CN 201610899052 A CN201610899052 A CN 201610899052A CN 107954438 A CN107954438 A CN 107954438A
Authority
CN
China
Prior art keywords
mesoporous
molecular sieves
fau
preparation
fau molecular
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
CN201610899052.6A
Other languages
Chinese (zh)
Other versions
CN107954438B (en
Inventor
唐康健
滕加伟
朱俊华
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 Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
Original Assignee
China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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 Chemical Corp, Sinopec Shanghai Research Institute of Petrochemical Technology filed Critical China Petroleum and Chemical Corp
Priority to CN201610899052.6A priority Critical patent/CN107954438B/en
Publication of CN107954438A publication Critical patent/CN107954438A/en
Application granted granted Critical
Publication of CN107954438B publication Critical patent/CN107954438B/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
    • 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
    • C01B39/04Crystalline 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 using at least one organic template directing agent, e.g. an ionic quaternary ammonium compound or an aminated compound
    • 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
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/12Surface area
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)

Abstract

The present invention relates to one kind to lead directly to mesoporous FAU molecular sieves and preparation method thereof.The problems such as mainly solution conventional art can not connect in microporous mesoporous duct completely when preparation has mesoporous FAU molecular sieves, and mesopore orbit easily caves in.The present invention is by using secondary treatment method, microemulsion of the dipping rich in silicon/aluminium/FAU templates in mesopore molecular sieve, and by secondary crystallization, in mesopore molecular sieve inner surface epitaxial growth FAU molecular sieves, then generation has through-type mesoporous FAU molecular sieves.This method ideally solve the problems, such as it is mentioned above, its method can be used for prepare in a variety of straight-through mesopore molecular sieve industrial productions.

Description

Lead directly to mesoporous FAU molecular sieves and preparation method thereof
Technical field
The present invention relates to one kind to lead directly to mesoporous FAU molecular sieves and preparation method thereof.
Background technology
FAU structure molecular screens belong to micro porous molecular sieve series, belong to octahedrite class, including the X-type of low silica-alumina ratio and Y types.Its Skeleton is mainly made of alumino-silicate, has the secondary structure of double hexatomic rings and β cages, and β cages are connected by double hexatomic rings to be formed Three-dimensional spaciousness skeleton structure.The Y types of high silica alumina ratio have high selectivity, high hydrothermal stability, suitable acidity.60 years 20th century In generation, is used for catalytic cracking first by Linde companies, and shows excellent Catalytic Cracking Performance in FCC reactions behind, after And it is widely used in major industrial enterprises and institutions.FAU molecular sieves use sodium hydroxide or 4-propyl bromide etc. to be used as structure directing Agent, crystallization 6h-10d is prepared at 100-180 DEG C.The activated centre of micro porous molecular sieve is more inside duct.Molecular sieve master The longer diffusional resistance that can increase molecule inside its duct in duct, prevents target product molecule from diffusing out in time inside duct And secondary response finally occurs and generates other molecules.Therefore diffusion path is shortened, reduction diffusional resistance has great importance. Introduced in one piece of micro porous molecular sieve crystal it is mesoporous come reduce diffusional resistance, accelerate diffusion:That is, synthetic microporous-composite mesoporous is more The molecular screen material of level pore passage structure has become the hot spot studied at present.It is common synthesis multi-stage porous FAU molecular sieves method be The micropore template agent for promoting FAU skeletons to be formed not only is added in synthetic system, is additionally added the mesoporous template for inducing mesoporous formation, Including as the carbon black pellet of hard template, carbon nanotubes, charcoal-aero gel, polysaccharide compound etc. and as soft template sun from Organosilan of sub- polymer and amphiphatic molecule etc.;J.Garcia-Martinez etc. (J.Garcia-Martinez et al., Catal.Sci&tech, 2012,2,987) by introducing cetyl trimethylammonium bromide (CTAB), it is secondary with Y little crystal grains two Length prepares mesoporous FAU molecular sieves;Song et al. is using the synthesising mesoporous FAU molecular sieves (Song Lijuan of method that starch is added in synthesis Deng,《Petroleum technology and application》, 2015,33,288);What (He Yilong etc.《Petrochemical industry Journal of Chinese Universities》, 2015,28, Et al. 31) mesoporous FAU molecular sieves are prepared using etching alkaline solution method.Although above method can obtain mesoporous distribution, The use of mesoporous template not only increases the complication that cost also results in synthesis step, is not appropriate for industrializing.Although on also, The mesopore molecular sieve that various methods are prepared for FAU is stated, but the microporous mesoporous mesoporous FAU directly connected research hotspot and difficulty always Point, otherwise the method preparation process reported is complicated, it is necessary to introduce the surfactant of price costly, complicated large scale Template etc. make it that cost is high, and post processing is cumbersome and causes environmental pollution., the multi-stage porous of gained is not real meaning On directly connect.Therefore, also there is very big challenge, conventional synthesis process for preparing with the mesoporous FAU directly connected Limit development and the commercial Application of through-type mesoporous FAU molecular sieves.
The content of the invention
The technical problems to be solved by the invention, that is, of high cost, the mesoporous FAU molecular sieves knot of gained existing in the prior art A kind of the problem of low, the straight-through property of crystalline substance is poor, there is provided preparation method of new straight-through mesoporous FAU molecular sieves.After this method has Processing procedure is simple;Manufacturing cost is low (any mesopore molecular sieve can serve as directly connecting);It is environmental-friendly that (microemulsion is whole Dipping, has reached Zero discharge);The mesoporous FAU of gained reaches the features such as real microporous mesoporous unbounded connection.
In order to solve the above technical problems, the technical solution adopted by the present invention is as follows:
One kind leads directly to mesoporous FAU molecular sieves, and the micropore in its structure is directly connected with mesoporous, and the micropore is in mesopore orbit In.
In above-mentioned technical proposal, micropore in FAU molecular sieve structures is directly connected with mesoporous in mesoporous molecular sieve structure, And the micropore is present in the mesopore orbit.
In above-mentioned technical proposal, mesopore molecular sieve is the mesopore molecular sieve with straight channels, is SBA more preferably Or MCM series, it is further preferable that being SBA-15 or MCM-41 or MCM-48.
In above-mentioned technical proposal, the micropore is seamlessly connected with mesoporous wall, and micropore canals are parallel-oriented with mesopore orbit It is again shorter than mesopore orbit, so as to form micro-~mesoporous part directly connected.
It is described to lead directly to mesoporous FAU molecular sieves by be soaked containing the microemulsion of FAU molecular sieve stostes in above-mentioned technical proposal Stain is made into mesopore molecular sieve after crystallization, roasting.
The present invention also provides a kind of preparation method for leading directly to mesoporous FAU molecular sieves, comprise the following steps:
A) template, surfactant, water, silicon source, silicon source and organic solvent are mixed, prepares FAU molecular sieve microemulsions;
B) the FAU molecular sieve microemulsions of preparation are impregnated into mesopore molecular sieve and obtain precursor A;
C) at 90~260 DEG C, at autogenous pressures, FAU molecular sieve microemulsions in mesopore molecular sieve crystallization and be situated between Hole FAU molecular sieves;
D) roasted under the conditions of 300~600 DEG C 0.5~72 it is small when through-type mesoporous FAU molecular sieves are made.
In above-mentioned technical proposal, the FAU molecular sieves microemulsion is water in oil microemulsion.
In above-mentioned technical proposal, in the FAU molecular sieves microemulsion, template, surfactant and water are mixed into water phase, Silicon source, silicon source and organic solvent are mixed into oil phase, and mixing water phase and oil phase obtain microemulsion.
In above-mentioned technical proposal, the silicon source:Silicon source:The molar ratio of template is 10:1-10:1-3;Organic solvent and table The molar ratio of face activating agent and water is 2-20:1-10:1.
In above-mentioned technical proposal, the FAU molecular sieves microemulsion is 1 in mass ratio with mesopore molecular sieve:0.5~5
In above-mentioned technical proposal, the mesopore molecular sieve is the mesopore molecular sieve with straight channels.
In above-mentioned technical proposal, the mesoporous molecular is screened from SBA or MCM series;More preferably, channel diameter 2 ~8 nanometers.
In above-mentioned technical proposal, the mesopore molecular sieve is SBA-15 or MCM-41 or MCM-48.
In above-mentioned technical proposal, the mesopore molecular sieve can be synthesized by this area conventional technical means, its duct size The big minor adjustment of surfactant can be passed through.
In above-mentioned technical proposal, the silicon source is included selected from ethyl orthosilicate, butyl silicate, white carbon, waterglass It is at least one;Source of aluminium is included selected from aluminium isopropoxide, aluminum nitrate, at least one of boehmite;The organic solvent includes Selected from benzene, toluene, carbon number be more than 6 alkane at least one, the present invention one specific embodiment in, organic solvent is Toluene;The surfactant includes amphipathic molecule, amphipathic polyethers, the aminated compounds of C8~C18 selected from C8-C12 At least one, in an of the invention specific embodiment, surfactant is tri-n-octyl amine;The template is with Na2O,NaOH Or quaternary ammonium salt, it is preferably sodium hydroxide or 4-propyl bromide.
In above-mentioned technical proposal, the crystallization temperature is 100-180 DEG C, is preferably, 110 DEG C;Crystallization time is 6-48h, Preferably 24h.
The present invention allows the aqueous solution containing template completely into hydrophobic mesoporous hole using the method for microemulsion dipping In road, micropore crystallization is set to be carried out completely in mesopore orbit.Specifically, using mesopore molecular sieve inner wall epitaxial growth Method, during crystallization, a part of mesoporous wall serves as silicon source and enters microcellular structure, reaches micropore/mesoporous wall and is seamlessly connected;Crystallization During, FAU is slowly grown in " circle " mesoporous inner wall in a manner of LBL, finally spontaneous in mesopore orbit to construct along Jie The straight hole road in hole duct direction, the straight hole road in this direction is parallel-oriented with mesopore orbit and shorter than mesopore orbit, so form Micro-~mesoporous part directly connected.The template containing N, O is removed by roasting, that is, produces highly uniform mesoporous/micropore and connects Logical structure.Since whole process uses the method for complete wetting, the microemulsion of FAU is not unnecessary and needs the part of blowdown, greatly The big cost for reducing reaction, at the same it is also environmentally friendly.Achieve preferable technique effect.
Attached drawing and explanation
Fig. 1 is the high-resolution-ration transmission electric-lens figure of the straight-through mesoporous FAU molecular sieves prepared in embodiment one under the conditions of 110 DEG C. 2. the micropore canals and the 1. of a relatively loose mesopore orbit parallel with apparent 2nm with apparent 0.8nm fine and close in figure Row, and cover wherein, clearly disclose micropore and connected with the unbounded of mesoporous part.
Fig. 2 is the small angle X-ray diffraction spectrogram of the straight-through mesoporous FAU molecular sieves prepared in embodiment one under the conditions of 110 DEG C. What the mesoporous part that XRD discloses the material was ordered into, the main spy of the main diffraction peak of celled portion and the standard spectrogram of FAU It is consistent to levy peak.
Fig. 3 is the wide-angle X-ray diffraction curve of the straight-through mesoporous FAU molecular sieves prepared in embodiment one under the conditions of 110 DEG C. What the mesoporous part that XRD discloses the material was ordered into, the main spy of the main diffraction peak of celled portion and the standard spectrogram of FAU It is consistent to levy peak.
Below by embodiment, the invention will be further elaborated.
Embodiment
【Embodiment 1】
The preparation for leading directly to mesoporous FAU molecular sieves carries out according to the following steps:FAU water-in-oil microemulsions, hydroxide are prepared first The aqueous solution that sodium and tri-n-octyl amine are matched somebody with somebody is micro emulsion water phase, and ethyl orthosilicate (TEOS) and the toluene solution of aluminium isopropoxide are oil phase, Mixing water phase and an oil phase obtains clear microemulsion I.Si in microemulsion I:Al:The molar ratio of NaOH or TPABr is 10:1:10;First Benzene is 2 with the molar ratio of tri-n-octyl amine and water:1:1;Lower microemulsion I of normal temperature condition and baked SBA-15 is in mass ratio 0.3:1 dipping obtains precursor II.After when aging 6 is small at 60 DEG C, precursor II is loaded stainless steel cauldron, in 110 DEG C of conditions Under, crystallization 24 obtains the mesoporous FAU molecular sieves containing template when small.After product takes out, when roasting 6 is small under the conditions of 550 DEG C Obtain straight-through mesoporous FAU molecular sieves.
The mesoporous SBA-15 can be synthesized by this area conventional technical means.
【Embodiment 2-3】
According to the type of the method for embodiment 1, simply change mesopore molecular sieve, you can to leading directly to mesoporous FAU molecular sieves The distribution of mesoporous, micropore is adjusted, obtain different mesoporous/micropores than straight-through mesoporous FAU molecular sieves.
The mesoporous MCM series can be synthesized by this area conventional technical means.
【Embodiment 4】
According to the method for embodiment 1, simply change surfactant.
【Embodiment 5】
According to the method for embodiment 1, it is 4-propyl bromide simply to change template.
【Embodiment 6】
According to the method for embodiment 1, simply change the molar ratio of organic solvent and water.
【Comparative example 1-2】
According to the method for embodiment 1, simply change the water and oil balance of microemulsion, then can obtain mesoporous FAU molecular sieves, still Duct is disconnected.
Specific embodiment result and comparative example result see the table below
Embodiment 1-6
Embodiment 1 2 3 4 5 6
Synthesis temperature (DEG C) 110 110 110 110 110 110
Reaction time (h) 24 24 24 24 24 24
Calcination temperature (DEG C) 550 550 550 550 550 550
Mesopore molecular sieve type SBA-15 MCM-41 MCM-48 SBA-15 SBA-15 SBA-15
Than surface (m2/g) 310 310 300 290 330 280
Whether lead directly to It is It is It is It is It is It is
It is situated between/micro- (void ratio) 1.0 0.7 0.6 0.9 1.1 0.6
Surfactant Tri-n-octyl amine Tri-n-octyl amine Tri-n-octyl amine Octyl phenol Tri-n-octyl amine Tri-n-octyl amine
Template Sodium hydroxide Sodium hydroxide Sodium hydroxide Sodium hydroxide 4-propyl bromide Sodium hydroxide
Organic solvent/water 2:1 2:1 2:1 2:1 2:1 4:1
Comparative example 1-2
Comparative example 1 2
Synthesis temperature (DEG C) 110 110
Reaction time (h) 24 24
Calcination temperature (DEG C) 550 550
Microemulsion type Water oil is continuous Oil-in-water
With the presence or absence of mesoporous and FAU It is It is
Whether connect It is non- It is non-

Claims (10)

1. one kind leads directly to mesoporous FAU molecular sieves, it is characterised in that the micropore in its structure is directly connected with mesoporous, the micropore In mesopore orbit.
2. a kind of preparation method for leading directly to mesoporous FAU molecular sieves, comprises the following steps:
A) template, surfactant, water, silicon source, silicon source and organic solvent are mixed, prepares FAU molecular sieve microemulsions;
B) the FAU molecular sieve microemulsions of preparation are impregnated into mesopore molecular sieve and obtain precursor A;
C) at 90~260 DEG C, at autogenous pressures, FAU molecular sieve microemulsions in mesopore molecular sieve crystallization and obtain mesoporous FAU molecular sieves;
D) roasted under the conditions of 300~600 DEG C 0.5~72 it is small when through-type mesoporous FAU molecular sieves are made.
3. the preparation method according to claim 2 for leading directly to mesoporous FAU molecular sieves, it is characterised in that the FAU molecular sieves Microemulsion is water in oil microemulsion.
4. the preparation method of the straight-through mesoporous FAU molecular sieves according to Claims 2 or 3, it is characterised in that the FAU points In son sieve microemulsion, template, surfactant and water are mixed into water phase, and silicon source, silicon source and organic solvent are mixed into oil phase, mix Heshui phase and oil phase obtain microemulsion.
5. the preparation method according to claim 2 for leading directly to mesoporous FAU molecular sieves, it is characterised in that the silicon source:Aluminium Source:The molar ratio of template is 10:1-10:1-3;The molar ratio of organic solvent and surfactant and water is 2-20:1-10:1.
6. the preparation method according to claim 2 for leading directly to mesoporous FAU molecular sieves, it is characterised in that the FAU molecular sieves Microemulsion is 1 in mass ratio with mesopore molecular sieve:0.5~5.
7. the preparation method according to claim 2 for leading directly to mesoporous FAU molecular sieves, it is characterised in that the mesoporous molecular Sieve as the mesopore molecular sieve with straight channels.
8. the preparation method of the straight-through mesoporous FAU molecular sieves according to claim 2 or 7, it is characterised in that described mesoporous point Son is screened from SBA or MCM series.
9. the preparation method for the straight-through mesoporous FAU molecular sieves stated according to claim 2, it is characterised in that the crystallization temperature is 100-180 DEG C, crystallization time 6-48h.
10. the preparation method according to claim 2 for leading directly to mesoporous FAU molecular sieves, it is characterised in that the silicon source includes Selected from ethyl orthosilicate, butyl silicate, white carbon, waterglass at least one;Source of aluminium is included selected from aluminium isopropoxide, nitre At least one of sour aluminium, boehmite;It is the alkane of more than 6 that the organic solvent, which is included selected from benzene, toluene, carbon number, It is at least one;The surfactant includes amphipathic molecule, amphipathic polyethers, the amine of C8~C18 selected from C8-C 12 At least one of compound;The template is Na2O, NaOH or quaternary ammonium salt.
CN201610899052.6A 2016-10-14 2016-10-14 Straight-through mesoporous FAU molecular sieve and preparation method thereof Active CN107954438B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610899052.6A CN107954438B (en) 2016-10-14 2016-10-14 Straight-through mesoporous FAU molecular sieve and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610899052.6A CN107954438B (en) 2016-10-14 2016-10-14 Straight-through mesoporous FAU molecular sieve and preparation method thereof

Publications (2)

Publication Number Publication Date
CN107954438A true CN107954438A (en) 2018-04-24
CN107954438B CN107954438B (en) 2020-09-04

Family

ID=61953156

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610899052.6A Active CN107954438B (en) 2016-10-14 2016-10-14 Straight-through mesoporous FAU molecular sieve and preparation method thereof

Country Status (1)

Country Link
CN (1) CN107954438B (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001038223A1 (en) * 1999-11-23 2001-05-31 Universite Laval Mesoporous zeolitic material with microporous crystalline mesopore walls
US20010054549A1 (en) * 2000-03-11 2001-12-27 Korea Research Institute Of Chemical Technology Continuous process and apparatus for preparing inorganic materials employing microwave
CN101108736A (en) * 2006-07-21 2008-01-23 中国石油天然气集团公司 Method of manufacturing Y type molecular sieve having micropore and mesohole at the same time
CN101580247A (en) * 2009-05-21 2009-11-18 中国科学院上海硅酸盐研究所 Order mesoporous hollow zeolite material and one-step hydro-thermal synthesis method thereof
CN102390843A (en) * 2011-08-02 2012-03-28 复旦大学 Three-dimensional interconnected hierarchical-structured zeolite molecular sieve material and preparation method thereof
CN103100399A (en) * 2011-11-11 2013-05-15 中国石油化工股份有限公司 Preparation method of mesoporous-microporous composite molecular sieve
CN103101930A (en) * 2013-03-04 2013-05-15 上海师范大学 Ordered mesopore ZSM-5 molecular sieve and preparation method thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001038223A1 (en) * 1999-11-23 2001-05-31 Universite Laval Mesoporous zeolitic material with microporous crystalline mesopore walls
US20010054549A1 (en) * 2000-03-11 2001-12-27 Korea Research Institute Of Chemical Technology Continuous process and apparatus for preparing inorganic materials employing microwave
CN101108736A (en) * 2006-07-21 2008-01-23 中国石油天然气集团公司 Method of manufacturing Y type molecular sieve having micropore and mesohole at the same time
CN101580247A (en) * 2009-05-21 2009-11-18 中国科学院上海硅酸盐研究所 Order mesoporous hollow zeolite material and one-step hydro-thermal synthesis method thereof
CN102390843A (en) * 2011-08-02 2012-03-28 复旦大学 Three-dimensional interconnected hierarchical-structured zeolite molecular sieve material and preparation method thereof
CN103100399A (en) * 2011-11-11 2013-05-15 中国石油化工股份有限公司 Preparation method of mesoporous-microporous composite molecular sieve
CN103101930A (en) * 2013-03-04 2013-05-15 上海师范大学 Ordered mesopore ZSM-5 molecular sieve and preparation method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
陆雪峰等: "具有微-介孔的分子筛复合材料的研究现状", 《内蒙古石油化工》 *

Also Published As

Publication number Publication date
CN107954438B (en) 2020-09-04

Similar Documents

Publication Publication Date Title
Kianfar Nanozeolites: synthesized, properties, applications
Chen et al. Hierarchically structured zeolites: synthesis, mass transport properties and applications
JP3163272B2 (en) Composition containing crystalline material and method for producing crystalline molecular sieve material
CN104226360B (en) Holocrystalline ZSM-5 molecular sieve catalyst and its production and use
CN104646050B (en) A kind of hydrogenation catalyst and its preparation and application
Zhou et al. Dual‐Mesoporous ZSM‐5 Zeolite with Highly b‐Axis‐Oriented Large Mesopore Channels for the Production of Benzoin Ethyl Ether
CN106732761A (en) The composite molecular screens of Beta SBA 16 and its obtained Hydrobon catalyst
CN105621445B (en) A kind of NaY types molecular sieve and preparation method thereof
CN106745036A (en) With the microporous mesoporous molecular sieves of multi-stage porous SSZ 13 and its synthetic method and application
CN104525246B (en) A kind of preparation method and applications of 5 catalyst of Template-free method little crystal grain Zn ZSM
CN108821304B (en) High-activity hierarchical pore titanium silicalite molecular sieve and preparation method and application thereof
CN106807437A (en) A kind of catalyst and its preparation and application that propylene is prepared for propane direct dehydrogenation
CN106830003A (en) SSZ-13/SCM-9 composite molecular screens and its synthetic method
CN102910644A (en) Multistage pore ZSM-5 molecular sieve and preparation method thereof
CN105645428B (en) The preparation method of the molecular sieves of SSZ 32 with mesoporous micropore graded structure
CN101767797B (en) Synthesizing method of mesoporous zeolite
Sun et al. Synthesis and hydrogen isomerization performance of ordered mesoporous nanosheet SAPO-11 molecular sieves
CN106082263A (en) A kind of preparation method of nano-hollow ZSM 5 molecular sieve in the rich hole of shell
CN107954438A (en) Lead directly to mesoporous FAU molecular sieves and preparation method thereof
CN107954448A (en) Mesoporous-SAPO-34 molecular sieves of straight channels and preparation method thereof
CN110342533B (en) Molecular sieve and preparation method and application thereof
CN107032368A (en) A kind of MTW Zeolitic NanoRods with symbiotic structure and preparation method thereof
CN107954444A (en) Lead directly to mesoporous ZSM-5 molecular sieve and preparation method thereof
Liu et al. A facile strategy of preparing nanosized NaY zeolite by stimulating negative crystals to accelerate the formation of D6R units
CN111056561B (en) Small-grain SSZ-13 molecular sieve containing hierarchical pores and synthesis method thereof

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