CN105565339A - Preparation method of small-crystalline-grain ZSM-22 (Zeolite Socony Mobil-22) molecular sieve - Google Patents

Preparation method of small-crystalline-grain ZSM-22 (Zeolite Socony Mobil-22) molecular sieve Download PDF

Info

Publication number
CN105565339A
CN105565339A CN201610119519.0A CN201610119519A CN105565339A CN 105565339 A CN105565339 A CN 105565339A CN 201610119519 A CN201610119519 A CN 201610119519A CN 105565339 A CN105565339 A CN 105565339A
Authority
CN
China
Prior art keywords
molecular sieve
preparation
zsm
fine grain
mixture
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
CN201610119519.0A
Other languages
Chinese (zh)
Other versions
CN105565339B (en
Inventor
李德宝
郗宏娟
侯博
林明桂
贾丽涛
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.)
Shanxi Institute of Coal Chemistry of CAS
Original Assignee
Shanxi Institute of Coal Chemistry 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 Shanxi Institute of Coal Chemistry of CAS filed Critical Shanxi Institute of Coal Chemistry of CAS
Priority to CN201610119519.0A priority Critical patent/CN105565339B/en
Publication of CN105565339A publication Critical patent/CN105565339A/en
Application granted granted Critical
Publication of CN105565339B publication Critical patent/CN105565339B/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
    • 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
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/62Submicrometer sized, i.e. from 0.1-1 micrometer
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/64Nanometer sized, i.e. from 1-100 nanometer

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)
  • Catalysts (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)

Abstract

The invention discloses a preparation method of a small-crystalline-grain ZSM-22 (Zeolite Socony Mobil-22) molecular sieve. The preparation method comprises the following steps of uniformly mixing a silicon source, a aluminum source, an alkali source, a templating agent and deionized water, to form an initial gel mixture, and then adding one or several of active carbon, graphite, graphene, black carbon, a starch microsphere, chitosan and a polylactic acid microsphere into the initial gel mixture, uniformly agitating an obtained mixture, and then crystallizing the agitated mixture, filtering to separate a solid product, washing the solid product to be neutral by using the deionized water, and drying and roasting the washed solid product, to obtain the small-crystalline-grain ZSM-22 molecular sieve. The preparation method has the advantages that the activity of a catalyst is high; the large-scale industrial production can be realized; the operation charge is low.

Description

A kind of preparation method of fine grain ZSM-5-22 molecular sieve
Affiliated field
The present invention relates to a kind of preparation method of fine grain ZSM-5-22 Si-Al molecular sieve.
Background technology
ZSM-22 molecular sieve is Mobil company of the U.S. in a kind of micropore, the high-silica zeolite of eighties of last century exploitation the late nineteen eighties, belongs to TON topological framework.It only has the duct of the one dimension of ten-ring opening, and port size is 0.44nm × 0.55nm, and port size is smaller, and without intersection duct.Because ZSM-22 molecular sieve has the pore passage structure and acidic nature be comparatively applicable to, in normal alkane isomerization reaction, have good catalytic performance, at petrochemical industry, particularly the aspect such as lubricant base isomerization dewaxing has been widely applied.
In lubricant base, the main component of wax is high-melting-point long-chain n-praaffin, and its pour point is high, and low temperature flowability is poor.By hydroisomerization reaction, normal paraffin is converted into branched paraffin, these performances can be improved.The isomerization of long chain alkane is reacted in the aperture of ZSM-22 molecular sieve by aperture catalysis and key lock catalytic mechanism.But the pattern of ZSM-22 molecular sieve is club shaped structure, and its length generally can reach 1 ~ 3 μm.Therefore, being only positioned at the activity of the active centre near molecular sieve aperture to catalyzer has contribution, and high catalyst activity requires that catalyzer has the aperture of more exposures.Improve the effective ways exposing aperture number and have two kinds: the mesopore orbit (2 ~ 50nm) that 1, manufacturing dimension is larger in zeolite crystal, form hierarchical porous structure; 2, the grain-size of molecular sieve is reduced.
At present, by preparing multi-stage porous ZSM-22 molecular sieve, to improve the report of catalyst performance more.Sinopec Group discloses the method that three kinds (CN102464325B, CN102874829B and CN102874830B) prepare mesopore-micropore zeolite molecular sieve material.First method CN102464325B is: in the enclosed system containing lower molecular weight organic solvent, first processes micro-pore zeolite (as ZSM-22) with alkaline solution; Then, with acid solution, micro-pore zeolite is processed, through being separated, washing and drying, finally obtain mesoporous-microporous zeolite.Second method CN102874829B introduces ultrasonication method, and detailed process is: first, is mixed by micro-pore zeolite (as ZSM-22), carry out ultrasonication with alkaline solution; Then, in the presence of an organic, in enclosed system, micro-pore zeolite is heat-treated; With acid solution, micro-pore zeolite is processed again, finally obtain mesoporous-microporous zeolite molecular sieve.The third method CN102874830B introduces microwave treatment method, detailed process is: micro-pore zeolite (as ZSM-22), alkaline solution and organic solvent are mixed, and carry out microwave treatment, and then carry out acid treatment, through being separated, washing and drying, finally obtain mesoporous-microporous zeolite.Although these three kinds of methods effectively can both prepare mesoporous-microporous zeolite molecular sieve, but the use of organic solvent and acid-base solution has increased considerably operation and the difficulty of liquid waste disposal, make its processing costs high, ultrasonic wave and microwave treatment have some limitations in large-scale industrial production in addition.
The ZSM-22 molecular sieve of synthesizing small-grain can obtain the aperture of more exposures, and catalyst activity is increased, and has no relevant report through retrieval.
Summary of the invention
The object of the present invention is to provide a kind of catalyst activity high, can large-scale industrial production, fine grain ZSM-5-22 molecular sieve preparation method that process cost is low.
The present invention is in ZSM-22 building-up process, by adding Graphene, spherex, chitosan, polylactic acid microsphere, gac, carbon black, graphite etc., there is the material being easily adsorbed in ZSM-22 molecular sieve aperture place feature, reaching and suppressing ZSM-22 grain growing thus the object obtaining small crystal grain molecular sieve.
Preparation method's concrete steps of the present invention are as follows:
(1) silicon source, aluminium source, alkali source, template and deionized water are mixed, form the initial gel mixture with following mol ratio, silicon source is with SiO 2meter, aluminium source is with Al 2o 3meter, alkali source is with OH -meter, SiO 2: Al 2o 3: template: OH -: deionized water=1:0.003-0.05:0.005-1.0:0.005-1.0:1-100;
(2) in step (1) gained initial gel mixture, add one or more in gac, graphite, Graphene, carbon black, spherex, chitosan, polylactic acid microsphere, and stir, wherein, SiO in the add-on of these materials and initial gel mixture 2mass ratio be: 0.001-2.0:1;
(3) mixture step (2) obtained in 120-200 DEG C, crystallization 4-144h under autogenous pressure;
(4) after crystallization completes, by solid product filtering separation, with deionized water wash to neutral, fine grain ZSM-5-22 molecular sieve after drying and roasting, is namely obtained; Wherein, maturing temperature is 400-600 DEG C, and roasting time is 5-40h.
Silicon source described above is a kind of or several arbitrarily mixture in silicon sol, Silica hydrogel, methyl silicate, tetraethoxy, white carbon black; Described aluminium source is mixture a kind of or several arbitrarily in pseudo-boehmite, aluminum chloride, Tai-Ace S 150, aluminum nitrate, aluminum isopropylate, sodium aluminate; The template adopted is one or more in diamines, N-methylimidazole bi-quaternary ammonium salt, diethylamine, n-Butyl Amine 99,1,8-diamino-octane of 1-ethylpyridine bromide, 1,6-; Described alkali source is one or both the mixture in sodium hydroxide, potassium hydroxide.
The present invention can also add crystal seed in step (1) starting sol, and crystal seed is filtered, washing, the dry stoste containing ZSM-22 crystal seed, also can be the former powder of ZSM-22.The addition of crystal seed is SiO 2the 0.1-10% of quality.
In step described above (3), crystal pattern is static under pressure itself or dynamic crystallization.
The crystal particle diameter of ZSM-22 molecular sieve prepared by method described above can be contracted to <300nm.Relative to traditional long particle diameter ZSM-22, there is higher catalytic activity.Such as: in n-dodecane hydroisomerization process, under the same reaction conditions, when n-dodecane transformation efficiency all reaches 90%, on traditional Pt/ZSM-22 molecular sieve, isomerisation selectivity is 63.1%, and on the Pt/ZSM-22 small crystal grain molecular sieve that the inventive method obtains, isomerisation selectivity can reach 75.1%.
Compared with prior art, the technology of the present invention can realize the synthesis of fine grain ZSM-5-22 in ZSM-22 molecular sieve process, without the need to adding acid-base solution again and organic solvent carries out pore-creating aftertreatment after ZSM-22 synthesis.Process of the present invention has the features such as simple to operate, with low cost, environmental friendliness, and gained ZSM-22 zeolite product has the advantages that crystal grain is little, catalytic activity is high, has good catalytic applications prospect.
Accompanying drawing explanation
Fig. 1 is the XRD spectra of comparative example product.
Fig. 2 is that the SEM of comparative example product is according to figure.
Fig. 3 is the XRD spectra of embodiment 1 product.
Fig. 4 is that the SEM of embodiment 1 product is according to figure.
Embodiment
Below by embodiment in detail the present invention is described in detail, but the present invention is not limited to these embodiments.
Comparative example 1:
First, mixed by following mol ratio by raw material, silicon sol is (with SiO 2meter): Tai-Ace S 150 is (with Al 2o 3meter): 1,6-is diamines: potassium hydroxide: deionized water=1:0.011:0.30:0.29:40.Then, mixing raw material is transferred in stainless steel cauldron, 160 DEG C of dynamic crystallization 48h, product is through filtration, washing, dry, 550 DEG C of roasting 16h, namely obtain conventional ZSM-22 molecular sieve, crystal grain length ~ 2 μm, Fig. 1 is shown in by XRD spectra and the SEM photo of product.
Embodiment 1:
First, mixed by following mol ratio by raw material, silicon sol is (with SiO 2meter): Tai-Ace S 150 is (with Al 2o 3meter): 1,6-is diamines: potassium hydroxide: deionized water=1:0.011:0.005:0.29:40.Then, add 0.5g gac (with add SiO 2mass ratio be 0.06:1), add the former powder of ZSM-22 (addition is 10% of SiO2 quality).Stir.Finally, mixing raw material is transferred in stainless steel cauldron, 160 DEG C of dynamic crystallization 48h, product is through filtration, washing, dry, 550 DEG C of roasting 16h, namely obtain the ZSM-22 molecular sieve of little crystal grain, crystal grain length ~ 200nm, XRD and the SEM spectrogram of product is shown in Fig. 2.
Embodiment 2-8:
Concrete proportion scale and crystallization condition are in table 1, and concrete preparation process is with embodiment 1.Wherein, the crystal seed that embodiment 2 adds is the stoste containing ZSM-22 crystal seed, and addition is SiO 20.1% of quality.The crystal seed that embodiment 3 adds is the former powder of ZSM-22, and addition is SiO 210% of quality.Embodiment 4-9, does not add crystal seed.
Synthetic sample does XRD analysis, data results and Fig. 1 close, show that synthetic product is high purity ZSM-22 molecular sieve.Synthetic sample does sem analysis, can find out that product is small crystal grain molecular sieve, Chang Du≤220nm.
Table 1 Zeolite synthesis batching and crystallization, roasting condition

Claims (8)

1. a preparation method for fine grain ZSM-5-22 molecular sieve, is characterized in that comprising the steps:
Silicon source, aluminium source, alkali source, template and deionized water are mixed, form the initial gel mixture with following mol ratio, silicon source is with SiO 2meter, aluminium source is with Al 2o 3meter, alkali source is with OH -meter, SiO 2: Al 2o 3: template: OH -: deionized water=1:0.003-0.05:0.005-1.0:0.005-1.0:1-100;
To in step (1) gained initial gel mixture, add one or more in gac, graphite, Graphene, carbon black, spherex, chitosan, polylactic acid microsphere, and stir, wherein, SiO in the add-on of these materials and initial gel mixture 2mass ratio be: 0.001-2.0:1;
Mixture step (2) obtained is in 120-200 oc, crystallization 4-144h under autogenous pressure;
After crystallization completes, by solid product filtering separation, with deionized water wash to neutral, after drying and roasting, namely obtain fine grain ZSM-5-22 molecular sieve; Wherein, maturing temperature is 400-600 oc, roasting time is 5-40h.
2. the preparation method of a kind of fine grain ZSM-5-22 molecular sieve as claimed in claim 1, is characterized in that adding crystal seed in step (1) starting sol, and crystal seed is filtered, washing, the dry stoste containing ZSM-22 crystal seed, or the former powder of ZSM-22.
3. the preparation method of a kind of fine grain ZSM-5-22 molecular sieve as claimed in claim 2, is characterized in that described seed load is SiO 2the 0.1-10% of quality.
4. the preparation method of a kind of fine grain ZSM-5-22 molecular sieve as described in any one of claim 1-3, is characterized in that described silicon source is a kind of or several arbitrarily mixture in silicon sol, Silica hydrogel, methyl silicate, tetraethoxy, white carbon black.
5. the preparation method of a kind of fine grain ZSM-5-22 molecular sieve as described in any one of claim 1-3, is characterized in that described aluminium source is mixture a kind of or several arbitrarily in pseudo-boehmite, aluminum chloride, Tai-Ace S 150, aluminum nitrate, aluminum isopropylate, sodium aluminate.
6. the preparation method of a kind of fine grain ZSM-5-22 molecular sieve as described in any one of claim 1-3, it is characterized in that described template is 1-ethylpyridine bromide, 1, one or more in diamines, N-methylimidazole bi-quaternary ammonium salt, diethylamine, n-Butyl Amine 99,1,8-diamino-octane of 6-.
7. the preparation method of a kind of fine grain ZSM-5-22 molecular sieve as described in any one of claim 1-3, is characterized in that described alkali source is one or both the mixture in sodium hydroxide, potassium hydroxide.
8. the preparation method of a kind of fine grain ZSM-5-22 molecular sieve as described in any one of claim 1-3, is characterized in that in described step (3), crystal pattern is static or dynamic crystallization.
CN201610119519.0A 2016-03-02 2016-03-02 A kind of preparation method of -22 molecular sieve of fine grain ZSM-5 Active CN105565339B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610119519.0A CN105565339B (en) 2016-03-02 2016-03-02 A kind of preparation method of -22 molecular sieve of fine grain ZSM-5

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610119519.0A CN105565339B (en) 2016-03-02 2016-03-02 A kind of preparation method of -22 molecular sieve of fine grain ZSM-5

Publications (2)

Publication Number Publication Date
CN105565339A true CN105565339A (en) 2016-05-11
CN105565339B CN105565339B (en) 2018-11-23

Family

ID=55876060

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610119519.0A Active CN105565339B (en) 2016-03-02 2016-03-02 A kind of preparation method of -22 molecular sieve of fine grain ZSM-5

Country Status (1)

Country Link
CN (1) CN105565339B (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106115733A (en) * 2016-06-20 2016-11-16 山东欧铂新材料有限公司 A kind of preparation method of multi-stage porous mordenite molecular sieve
CN106475131A (en) * 2016-10-11 2017-03-08 中国科学院山西煤炭化学研究所 A kind of Graphene/molecular sieve composite catalyst and preparation method thereof
CN106587100A (en) * 2016-10-25 2017-04-26 浙江大学 Method for synthesizing laminar ZSM-5 zeolite molecular sieve with single micro-molecule organic template
CN108470594A (en) * 2018-03-14 2018-08-31 清华大学 A method of it is added dropwise and prepares simulation pollucite source core
CN111410207A (en) * 2020-03-12 2020-07-14 青岛科技大学 Normal-pressure synthesis method of SAPO-11 molecular sieve
CN111422881A (en) * 2020-04-10 2020-07-17 吉林大学 TON type zeolite molecular sieve and preparation method thereof
CN113023747A (en) * 2021-03-31 2021-06-25 南京工业大学 TON zeolite with fractal structure and preparation method thereof
CN113233472A (en) * 2021-06-11 2021-08-10 福州大学 Synthesis method of nano small-grain ZSM-22 molecular sieve
CN114160193A (en) * 2021-12-06 2022-03-11 厦门大学 CoAPO-11 molecular sieve, preparation method and application thereof, alkane hydroisomerization catalyst and application thereof
CN116212961A (en) * 2023-02-15 2023-06-06 南宁师范大学 Preparation method for forming mesoporous structure by adjusting and controlling ZIF-67 through ZSM-5 seed crystal

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103183354A (en) * 2011-12-31 2013-07-03 上海欣年石化助剂有限公司 Method for preparing EUO structural zeolite
CN104787777A (en) * 2015-03-20 2015-07-22 中国石油天然气股份有限公司 Highly-dispersed small grain ZSM-5 zeolite and preparation method thereof

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103183354A (en) * 2011-12-31 2013-07-03 上海欣年石化助剂有限公司 Method for preparing EUO structural zeolite
CN104787777A (en) * 2015-03-20 2015-07-22 中国石油天然气股份有限公司 Highly-dispersed small grain ZSM-5 zeolite and preparation method thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
XIAOTONG WEI ET AL.: ""Synthesis and characterization of mesoporous ZSM-12 by using carbon particles"", 《MICROPOROUS AND MESOPOROUS MATERIALS》 *
许宁 等: ""高硅分子筛ZSM-22的动态合成及表征"", 《催化学报》 *
霍志萍 等: ""ZSM-22分子筛合成研究进展"", 《工业催化》 *

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106115733A (en) * 2016-06-20 2016-11-16 山东欧铂新材料有限公司 A kind of preparation method of multi-stage porous mordenite molecular sieve
CN106475131A (en) * 2016-10-11 2017-03-08 中国科学院山西煤炭化学研究所 A kind of Graphene/molecular sieve composite catalyst and preparation method thereof
CN106475131B (en) * 2016-10-11 2019-01-11 中国科学院山西煤炭化学研究所 A kind of graphene/molecular sieve composite catalyst and preparation method thereof
CN106587100A (en) * 2016-10-25 2017-04-26 浙江大学 Method for synthesizing laminar ZSM-5 zeolite molecular sieve with single micro-molecule organic template
CN106587100B (en) * 2016-10-25 2018-09-21 浙江大学 The method for synthesizing laminar ZSM-5 zeolite molecular sieve with single small molecule organic formwork agent
CN108470594A (en) * 2018-03-14 2018-08-31 清华大学 A method of it is added dropwise and prepares simulation pollucite source core
CN111410207A (en) * 2020-03-12 2020-07-14 青岛科技大学 Normal-pressure synthesis method of SAPO-11 molecular sieve
CN111410207B (en) * 2020-03-12 2022-11-25 青岛科技大学 Normal-pressure synthesis method of SAPO-11 molecular sieve
CN111422881B (en) * 2020-04-10 2021-11-05 吉林大学 TON type zeolite molecular sieve and preparation method thereof
CN111422881A (en) * 2020-04-10 2020-07-17 吉林大学 TON type zeolite molecular sieve and preparation method thereof
CN113023747A (en) * 2021-03-31 2021-06-25 南京工业大学 TON zeolite with fractal structure and preparation method thereof
CN113233472B (en) * 2021-06-11 2022-06-07 福州大学 Synthesis method of nano small-grain ZSM-22 molecular sieve
CN113233472A (en) * 2021-06-11 2021-08-10 福州大学 Synthesis method of nano small-grain ZSM-22 molecular sieve
CN114160193A (en) * 2021-12-06 2022-03-11 厦门大学 CoAPO-11 molecular sieve, preparation method and application thereof, alkane hydroisomerization catalyst and application thereof
CN114160193B (en) * 2021-12-06 2023-04-07 厦门大学 CoAPO-11 molecular sieve, preparation method and application thereof, alkane hydroisomerization catalyst and application thereof
CN116212961A (en) * 2023-02-15 2023-06-06 南宁师范大学 Preparation method for forming mesoporous structure by adjusting and controlling ZIF-67 through ZSM-5 seed crystal

Also Published As

Publication number Publication date
CN105565339B (en) 2018-11-23

Similar Documents

Publication Publication Date Title
CN105565339A (en) Preparation method of small-crystalline-grain ZSM-22 (Zeolite Socony Mobil-22) molecular sieve
US10099931B2 (en) One-step preparation method for hollow shell type small grain ZSM-5 molecular sieve
CN102826565B (en) Preparation method of multi-stage pore channel beta molecular screen
CN104556094B (en) A kind of Y/Silicalite-1 composite molecular screen and preparation method thereof
CN102190316B (en) Method for synthesizing mesoporous mordenite
CN109467099A (en) A kind of preparation method of nanoscale pure silicon step hole Beta molecular sieve
CN105032478B (en) A kind of catalyst and its dedicated core-shell structure compound molecular sieve for the oily isomerization-visbreaking of F-T synthetic middle distillates point
CN104043477B (en) ZSM-5/MCM-48 composite molecular sieve, preparation method and application thereof
CN105645427B (en) The preparation method of the molecular sieves of ZSM 22 with mesoporous micropore graded structure
CN111017950A (en) Preparation method and application of low-cost SSZ-13 molecular sieve
CN106044793A (en) Method for synthesis of nanometer ZSM-5 molecular sieve from mother liquor flocculate
CN114436279B (en) ZSM-22 molecular sieve, preparation method and application thereof, and n-dodecane isomerization reaction
CN105948073A (en) Preparation method of SAPO-34 molecular sieve
CN114471672A (en) Catalyst for alkylation of benzene and ethylene, preparation method and application thereof
CN102060308A (en) Synthesis method of nano fibrous mordenite
CN106082263A (en) A kind of preparation method of nano-hollow ZSM 5 molecular sieve in the rich hole of shell
CN107032368B (en) A kind of MTW Zeolitic NanoRods and preparation method thereof with symbiotic structure
CN106276967B (en) A kind of synthetic method of mesoporous zeolite
CN101353171A (en) Method for synthesis of beta-zeolite
CN115010146B (en) Multistage hole ZSM-5 nano aggregate molecular sieve and preparation method thereof
CN105883848A (en) Method for preparing hierarchical porous ZSM-5 zeolite microspheres through recycling of crystallization liquid
CN110203937B (en) Synthesis method of cubic phase ordered ultramicropore silicon dioxide
CN107511165A (en) The preparation method of binder free mercerising molecular sieve catalyst
CN115140746B (en) ZSM-5 molecular sieve with cascade hole distribution and preparation method thereof
CN106698454A (en) Nanometer EU-1 molecular sieve synthesizing method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant