CN102001681A - Method for synthesizing ZSM-5 zeolite - Google Patents

Method for synthesizing ZSM-5 zeolite Download PDF

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CN102001681A
CN102001681A CN 201010546164 CN201010546164A CN102001681A CN 102001681 A CN102001681 A CN 102001681A CN 201010546164 CN201010546164 CN 201010546164 CN 201010546164 A CN201010546164 A CN 201010546164A CN 102001681 A CN102001681 A CN 102001681A
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zeolite
synthetic method
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肖强
庄津
刘刚
许春慧
张富民
钟依均
朱伟东
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Zhejiang Normal University CJNU
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Abstract

The invention relates to a method for synthesizing ZSM-5 zeolite with a multi-stage porous structure under the action of a silane coupling agent, and aims to provide the method for synthesizing the ZSM-5 zeolite, which has a simple crystallization process and low production cost, aiming at the defects of complex crystallization process and low production cost existing in the conventional process for synthesizing the ZSM-5 zeolite with multi-stage porous structure. The technical scheme of the invention is that: tetrapropyl ammonium bromide is used as a template agent, water glass is used as a silicon source and aluminum sulfate is used as an aluminum source; and a commercial silane coupling agent is directly added into the conventional ZSM-5 zeolite synthesis system. The method comprises the following steps of: (1) adding the silicon source into water and dissolving; (2) adding the silane coupling agent and stirring; (3) adding the template agent and the aluminum source; (4) adding an acid; (5) stirring the mixture obtained in the steps (1) to (4) and crystallizing; (6) filtering, washing and drying to obtain a template agent-containing product; and (7) drying the template agent-containing product and baking at the temperature of between 400 and 650 DEG C for 3 to 10 hours to obtain the zeolite product with multi-stage porous structure.

Description

A kind of synthetic method of ZSM-5 zeolite
Technical field
The present invention relates to a kind of synthetic method of ZSM-5 zeolite, particularly a kind of synthesizing under the silane coupling agent effect has the method for hierarchical porous structure ZSM-5 zeolite.
Background technology
Zeolite molecular sieve is the crystal aluminosilicate material that a class has regular microvoid structure, with its high-specific surface area, high absorption capacity, high hydrothermal stability and characteristics such as micropore canals with shape selective, all be widely used in fields such as petrochemical complex, refining of petroleum, fractionation by adsorption, the synthetic chemistry of zeolite molecular sieve and industrial application are subjected to the great attention of academia and industrial community all the time.
The catalytic active center of zeolite mainly is positioned at its micropore canals inside, and its duct size is generally between 0.3~1.0nm.The diffusion of molecule in micropore canals belongs to configuration diffusion (configurational diffusion), rate of diffusion is slower, the active centre of molecule from the zeolite crystal surface diffusion to crystals exists very strong restriction, and this just greatly reduces the effective rate of utilization of zeolite.The hierarchical porous structure zeolite generally refers to except that the zeolite micropore duct, also has the zeolite molecular sieve of mesopore orbit system.Mesoporous existence can improve the mass-transfer performance of zeolite greatly, and the catalyzed reaction that macromole is participated in can show good catalytic performance.
The ZSM-5 zeolite molecular sieve is the high-silica zeolite with two-dimentional ten-ring pore passage structure of the seventies in last century by the exploitation of U.S. Mobil company, be one of present of paramount importance molecular sieve catalytic material, be widely used in fields such as refining of petroleum, Coal Chemical Industry and fine chemistry industry.Synthetic ZSM-5 zeolite with hierarchical porous structure, the mass-transfer performance of raising molecular sieve, significant for the catalytic efficiency that improves the ZSM-5 zeolite.
Document (Nature Materials, 2006,5,718-723) reported a kind of synthetic method of hierarchical porous structure ZSM-5 zeolite, concrete is that the silane coupled cats product of employing is a template, directly synthesized hole wall by the mesoporous ZSM-5 zeolite that zeolite is formed, mesoporous aperture is adjustable by hydrothermal crystallizing, the silicone surfactant of employing partly is made up of long chain quaternary part and methoxy silane, and the centre is connected by the Si-C key.(Angewandte Chemie International Edition 2006,45 7603-7606) has reported that a kind of to adopt the polymkeric substance of silane coupledization be the method for the synthesising mesoporous ZSM-5 of mesoporous template to document.But the mesoporous template of silane coupledization that is adopted not is a commercially produced product, is that mesoporous zeolite of template preparation is faced with the preparation process complexity, production cost is crossed problems such as height with it.
Silane coupling agent is the silane that a class has organo-functional group, and it is widely used in the modification of macromolecular material.It of a great variety, available general formula Y (CH 2) nSiX 3The expression (X is a methoxy or ethoxy, and Y is primary amine groups, quaternary ammonium group, chain alkyl etc.), in its molecule, have simultaneously can with the chemically combined reactive group of inorganic materials and with the chemically combined reactive group of organic materials.
U.S. Pat 5,194,410 have reported a kind of method of synthesizing the ZSM-5 zeolite molecular sieve under the organosilicon effect of quaternary ammonium salt functionalization.Organosilicon both as structure directing agent, provides part silicon source again in building-up process.Li Xiaotian etc. (SCI, 2000,21,683-685) also reported to be that structure directing agent has synthesized the ZSM-5 molecular sieve with the quaternary ammonium salt silane coupling agent.But this two portions work does not relate to the synthetic of hierarchical porous structure ZSM-5 zeolite.
People such as Serrano (Chemistry of Materials, 2006,18,2462-2464; 2009,21,641-654) the method for synthesis of nano ZSM-5 under a kind of silane coupling agent effect of report, this method is at first to make the pre-crystallization of synthetic system, and then adding silane coupling agent (as the phenylamino propyl trimethoxy silicane) continuation crystallization obtains the ZSM-5 molecular sieve with hierarchical porous structure of crystal grain less than 10nm.But the report that does not relate to pattern, to adopt expensive TPAOH (TPAOH) be template to this method in addition, adds silane coupling agent, crystallization process complexity in the middle of the crystallization process.
Summary of the invention
The objective of the invention is provides the synthetic method of the ZSM-5 zeolite that a kind of crystallization process is simple, production cost is low at having the existing crystallization process complexity of ZSM-5 zeolite of hierarchical porous structure, the weak point that production cost is high in existing synthesizing.
The technical scheme of the synthetic method of a kind of ZSM-5 zeolite of the present invention is: the synthetic method of ZSM-5 zeolite may further comprise the steps:
(1) the silicon source is added to the water dissolving;
(2) add silane coupling agent, stir;
(3) add template and aluminium source;
(4) add acid;
(5) after the mixture that step (1)-(4) obtain stirs, crystallization;
(6) obtain containing the product of template after filtration, washing, the drying;
(7) contain the product oven dry of template after, 400~650 ℃ of roastings promptly got in 3~10 hours has the hierarchical porous structure zeolite product.
In the synthetic method of above-mentioned ZSM-5 zeolite, the silicon source is a water glass.
In the synthetic method of above-mentioned ZSM-5 zeolite, template is 4-propyl bromide (TPABr).
In the synthetic method of above-mentioned ZSM-5 zeolite, the aluminium source is Tai-Ace S 150 (Al 2(SO 4) 318H 2O).
In the synthetic method of above-mentioned ZSM-5 zeolite, acid is sulfuric acid.
In the synthetic method of above-mentioned ZSM-5 zeolite, silane coupling agent is a kind of in aminopropyl triethoxysilane (APTES), aminopropyl trimethoxysilane (APTMS), (3-epoxy ethyl methoxy-propyl) Trimethoxy silane (GPTMS), the propyl-triethoxysilicane (PTES).
In the synthetic method of above-mentioned ZSM-5 zeolite, the reactant molar ratio scope of reaction system is: silane coupling agent: Si=0.025~0.1: 1, Na 2O: Si=0.05~0.1: 1, Al 2O 3: Si=0.01~0.025: 1, H 2O: Si=25: 1, TPABr: Si=0.2: 1.
In the synthetic method of above-mentioned ZSM-5 zeolite, in step (2), behind the adding silane coupling agent, stir more than 2 hours.
In the synthetic method of above-mentioned ZSM-5 zeolite, the time of stirring in step (5) is more than 2 hours.
In the synthetic method of above-mentioned ZSM-5 zeolite, carry out in autoclave in the crystallization described in the step (5), crystallization is finished at twice, directly carry out the crystallization second time after crystallization is finished for the first time, wherein, crystallization temperature is 100~150 ℃ for the first time, and crystallization time was less than 3 days; Crystallization temperature is 150~190 ℃ for the second time, and crystallization time is 1~10 day.
The ZSM-5 molecular sieve pattern that the present invention relates to is spherical, and has hierarchical porous structure.It is template that the present invention adopts 4-propyl bromide, be that silicon source, Tai-Ace S 150 are the aluminium source with water glass, the commercialization silane coupling agent directly joins in the synthetic system of ZSM-5 zeolite, synthesis material is simple and easy to, crystallization process is simple, and the ZSM-5 sample degree of crystallinity that obtains is higher, finds that simultaneously the adding of silane coupling agent can regulate the acidity of ZSM-5 zeolite.For the ZSM-5 zeolite molecular sieve for preparing hierarchical porous structure provides easy route of synthesis.
Description of drawings
Fig. 1 is embodiment 1 a sample powder X-ray diffractogram (XRD).
Fig. 2 is embodiment 1 sample scanning electron microscope microscope figure (SEM).
Fig. 3 is embodiment 1 sample-196 a ℃ following nitrogen adsorption isotherm.
Fig. 4 is embodiment 1 sample ammonia temperature programmed desorption(TPD) figure (NH 3-TPD).
Fig. 5 is embodiment 2 sample powder X-ray diffractograms (XRD).
Fig. 6 is embodiment 2 sample scanning electron microscope microscope figure (SEM).
Fig. 7 is embodiment 2 sample ammonia temperature programmed desorption(TPD) figure (NH 3-TPD).
Fig. 8 is embodiment 9 sample powder X-ray diffractograms (XRD).
Fig. 9 is embodiment 9 sample scanning electron microscope microscope figure (SEM).
Figure 10 is embodiment 9 samples-196 ℃ following nitrogen adsorption isotherm.
The specific examples mode
Below by some embodiment the synthetic method of a kind of ZSM-5 zeolite of the present invention is further described, but the present invention is not limited to these embodiment.
Embodiment 1
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.05APTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.443g APTES, 2.1301g TPABr, 5.0g Al 2(SO 4) 318H 2O and 1.7g H 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 1 day, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Fig. 1 is the x-ray diffractogram of powder (XRD) of embodiment 1 sample, and the XRD figure show sample has the MFI structure, and Fig. 2 is the SEM figure of embodiment 1 sample, and sample is spherical in shape, the about 5 μ m of diameter.Fig. 3 is the nitrogen adsorption isotherm under embodiment 1 sample-196 ℃, and it is at relative pressure P/P 0One hop is arranged, corresponding to N after being higher than 0.4 2The capillary condensation phenomenon of molecule in mesoporous, interpret sample has meso-hole structure.Fig. 4 is the NH of embodiment 1 sample 3-TPD figure has two peaks among the figure, correspond respectively to the desorption of weak acid and strong acidic site adsorb ammonia among the ZSM-5.
Embodiment 2
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.1APTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.886g APTES, 2.130g TPABr, 5.0gAl 2(SO 4) 318H 2O and 1.9g H 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 7 days, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Obtain XRD figure, SEM figure and the NH of product 3-TPD figure sees Fig. 5, Fig. 6 and Fig. 7 respectively.The synthetic sample has the MFI structure, and pattern is spherical, diameter between 16-20 μ m, NH 3Two peaks are arranged among-the TPD, correspond respectively to the desorption of weak acid and strong acidic site adsorb ammonia among the ZSM-5, obviously reduce with respect to strong acidic site quantity among the embodiment 1.
Embodiment 3
According to mole proportioning: 0.1Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.05APTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water and 0.443g APTES stirred 3 hours, adds 2.1301g TPABr, 5.0g Al again 2(SO 4) 318H 2O and 1.5g H 2SO 4(4.82mol/l), treat that gel mixture stirs after, earlier 110 ℃ of following crystallization are 2 days, again 180 ℃ of following crystallization 1 day, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Sample has the MFI structure, and spherical morphology, nitrogen adsorption characterize has meso-hole structure.
Embodiment 4
According to mole proportioning: 0.05Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.05APTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.443g APTES, 2.1301g TPABr, 5.0g Al (SO 4) 318H 2O and 1.9gH 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 1 day, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Sample has the MFI structure, and spherical morphology, nitrogen adsorption characterize has meso-hole structure.
Embodiment 5
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.025APTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.221g APTES, 2.1301g TPABr, 5.0g Al 2(SO 4) 318H 2O and 1.9g H 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 1 day, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Sample has the MFI structure, and spherical morphology, nitrogen adsorption characterize has meso-hole structure.
Embodiment 6
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.1APTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.886g APTES, 2.1301g TPABr, 5.0g Al 2(SO 4) 318H 2O and 1.9g H 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 3 days, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Sample has the MFI structure, and spherical morphology, nitrogen adsorption characterize has meso-hole structure.
Embodiment 7
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.1APTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.886g APTES, 2.1301g TPABr, 5.0g Al 2(SO 4) 318H 2O and 1.9g H 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 4 days, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Sample has the MFI structure, and spherical morphology, nitrogen adsorption characterize has meso-hole structure.
Embodiment 8
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.1APTMS adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.718g APTMS, 2.1301g TPABr, 5.0g Al 2(SO 4) 318H 2O and 1.9g H 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 6 days, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Sample has the MFI structure, and spherical morphology, nitrogen adsorption characterize has meso-hole structure.
Embodiment 9
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.05GPTMS adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.473g GPTMS, 2.130g TPABr, 5.0gAl 2(SO 4) 318H 2O and 1.9gH 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 1 day, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.The XRD figure, SEM figure and the nitrogen adsorption desorption thermoisopleth that obtain product are seen Fig. 8, Fig. 9 and Figure 10 respectively.The XRD figure show sample has the MFI structure, and SEM figure show sample is spherical in shape, the about 1 μ m of diameter.One hop after being higher than 0.4, relative pressure P/P0 is arranged, corresponding to N among the nitrogen adsorption isotherm figure 2The capillary condensation phenomenon of molecule in mesoporous, interpret sample has meso-hole structure.
Embodiment 10
According to mole proportioning: 0.07Na 2O: SiO 2: 0.025Al 2O 3: 25H 2O: 0.2TPABr: 0.05PTES adds 9g water glass (Na successively in reactor 2O:10.6wt.%; SiO 2: 26.5wt.%), 6.4ml deionized water, 0.825g PTES, 2.130g TPABr, 5.0gAl 2(SO 4) 318H 2O and 1.9g H 2SO 4(4.82mol/l), fully stir make gel mixture evenly after, 110 ℃ of following crystallization are 2 days earlier, again 180 ℃ of following crystallization 4 days, the crystallization product suction filtration, washing obtains white products after the drying.Sample was removed template in 6 hours 550 ℃ of following roastings.Sample has the MFI structure, and spherical morphology, nitrogen adsorption characterize has meso-hole structure.

Claims (10)

1. the synthetic method of a ZSM-5 zeolite, it is characterized in that: the synthetic method of this ZSM-5 zeolite may further comprise the steps:
(1) the silicon source is added to the water dissolving;
(2) add silane coupling agent, stir;
(3) add template and aluminium source;
(4) add acid;
(5) after the mixture that step (1)-(4) obtain stirs, crystallization;
(6) obtain containing the product of template after filtration, washing, the drying;
(7) contain the product oven dry of template after, 400~650 ℃ of roastings promptly got in 3~10 hours has the hierarchical porous structure zeolite product.
2. according to the synthetic method of right 1 described ZSM-5 zeolite, it is characterized in that described silicon source is a water glass.
3. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, it is characterized in that described template is 4-propyl bromide (TPABr).
4. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, it is characterized in that described aluminium source is Tai-Ace S 150 (Al 2(SO 4) 318H 2O).
5. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, it is characterized in that described acid is sulfuric acid.
6. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, it is characterized in that described silane coupling agent is a kind of in aminopropyl triethoxysilane (APTES), aminopropyl trimethoxysilane (APTMS), (3-epoxy ethyl methoxy-propyl) Trimethoxy silane (GPTMS), the propyl-triethoxysilicane (PTES).
7. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, it is characterized in that in the synthetic method of this ZSM-5 zeolite that the reactant molar ratio scope of reaction system is: silane coupling agent: Si=0.025~0.1: 1, Na 2O: Si=0.05~0.1: 1, Al 2O 3: Si=0.01~0.025: 1, H 2O: Si=25: 1, TPABr: Si=0.2: 1.
8. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, after it is characterized in that in step (2), adding silane coupling agent, stir more than 2 hours.
9. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, it is characterized in that the time of stirring is more than 2 hours in step (5).
10. according to the synthetic method of right 1 or 2 described ZSM-5 zeolites, it is characterized in that in autoclave, carrying out in the crystallization described in the step (5), crystallization is finished at twice, directly carry out the crystallization second time after crystallization is finished for the first time, wherein, crystallization temperature is 100~150 ℃ for the first time, and crystallization time was less than 3 days; Crystallization temperature is 150~190 ℃ for the second time, and crystallization time is 1~10 day.
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CN102530980A (en) * 2012-01-13 2012-07-04 大连理工大学 Hierarchical zeolite, preparation and application thereof
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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1631778A (en) * 2004-11-12 2005-06-29 南开大学 Fractional crystallization method for preparing organic functionalized micellization molecular sieve

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1631778A (en) * 2004-11-12 2005-06-29 南开大学 Fractional crystallization method for preparing organic functionalized micellization molecular sieve

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 20100915 宋丽萍 多级孔道沸石的合成及应用 32-46 1-10 , 第9期 2 *

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CN107840349A (en) * 2016-09-19 2018-03-27 中国石油化工股份有限公司 The preparation method of the nanometer multi-stage porous aggregations of ZSM 5
CN107840349B (en) * 2016-09-19 2020-07-07 中国石油化工股份有限公司 Preparation method of nano ZSM-5 hierarchical pore aggregate
CN108607600A (en) * 2016-12-10 2018-10-02 中国科学院大连化学物理研究所 A kind of catalyst of molecular sieve carried high dispersive noble metal and its preparation and application
CN108607600B (en) * 2016-12-10 2020-09-08 中国科学院大连化学物理研究所 Catalyst with high-dispersion noble metal loaded on molecular sieve, and preparation and application thereof
CN109395768A (en) * 2017-08-16 2019-03-01 王学彬 A kind of functionalization ZSM-5 molecular sieve
CN108178163A (en) * 2017-12-27 2018-06-19 中国石油大学(北京) A kind of low silicon multilevel hierarchy ZSM-5 zeolite molecular sieve and its preparation method and application
CN114426291A (en) * 2020-10-13 2022-05-03 中国石油化工股份有限公司 ZSM-5 zeolite molecular sieve and synthesis method and application thereof
CN114426291B (en) * 2020-10-13 2023-07-04 中国石油化工股份有限公司 ZSM-5 zeolite molecular sieve and synthesis method and application thereof
CN113023746A (en) * 2021-03-17 2021-06-25 宁夏大学 Lanthanum modified molecular sieve and preparation method and application thereof

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Application publication date: 20110406