CN110127718A - A kind of ZSM-35/ZSM-5 composite molecular screen and preparation method thereof - Google Patents

A kind of ZSM-35/ZSM-5 composite molecular screen and preparation method thereof Download PDF

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Publication number
CN110127718A
CN110127718A CN201910449975.5A CN201910449975A CN110127718A CN 110127718 A CN110127718 A CN 110127718A CN 201910449975 A CN201910449975 A CN 201910449975A CN 110127718 A CN110127718 A CN 110127718A
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China
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zsm
molecular sieve
composite molecular
molecular screen
silicon source
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Inventor
刘月明
沈凯旭
黄鑫
王佳
陈贞
余云开
唐智谋
王蕊
刘昊昕
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East China Normal University
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East China Normal University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/80Mixtures of different zeolites
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
    • C01B39/36Pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • C01B39/38Type ZSM-5
    • C01B39/40Type ZSM-5 using at least one organic template directing agent
    • 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
    • C01B39/44Ferrierite type, e.g. types ZSM-21, ZSM-35 or ZSM-38
    • C01B39/445Ferrierite type, e.g. types ZSM-21, ZSM-35 or ZSM-38 using at least one organic template directing agent
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/65Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the ferrierite type, e.g. types ZSM-21, ZSM-35 or ZSM-38, as exemplified by patent documents US4046859, US4016245 and US4046859, respectively
    • 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

Abstract

The invention discloses a kind of ZSM-35/ZSM-5 composite molecular screens and preparation method thereof, the composite molecular screen has the structure feature of FER topological structure and MFI topological structure molecular sieve simultaneously, the isopropylamine for generating ZSM-35 molecular sieve but also guiding generation ZSM-5 molecular sieve can be oriented to as template by using, and ZSM-35/ZSM-5 composite molecular screen is prepared in hydrothermal synthesis.Obtained composite molecular screen stable structure, composition is controllable, has excellent performance.Preparation method step is simple and convenient to operate, and is easy to industrial applications.

Description

A kind of ZSM-35/ZSM-5 composite molecular screen and preparation method thereof
Technical field
The invention belongs to field of chemical technology, it is related to a kind of composite molecular screen and preparation method thereof, specifically, being related to It is a kind of while there is ZSM-35 molecular sieve structure and the composite molecular screen of ZSM-5 molecular sieve structure and preparation method thereof.
Background technique
Composite molecular screen is the composite crystal formed by two or more different topology structure molecular sieve combination, generally It is able to maintain the self property of every kind of molecular sieve structure, while unique cellular structure and Acidity can also be generated, it is anti-in catalysis The feature different from single molecular sieve is shown in answering.CN94113403.2 discloses ZSM-5/ZSM-11 composite molecular screen, It is applied in catalytic cracked dry gas ethylbenzene reaction process as catalyst, shows and be substantially better than ZSM-5 molecular sieve catalyst Reactivity worth.In order to organically combine the characteristic of different topology structure molecular sieve to improve the catalytic perfomance of catalyst, grind The persons of studying carefully have developed a series of composite molecular screens in succession.CN1583562A discloses a kind of FAU/BEA double-micropore composite molecular sieve, CN106946268A discloses a kind of MOR/ZSM-35 composite molecular screen, and CN101003379A discloses a kind of ZSM-35/MCM- 22 composite molecular screens.Due to the particularity of compound molecule sieve structure, so composite molecular screen, which is provided with, is substantially better than single molecule The Acidity feature and cellular structure feature of sieve, can overcome the limitation of single molecular sieve self structure, can preferably meet combustion The demand of material and chemicals production chemical process industrial applications, has broad application prospects.
ZSM-35 molecular sieve has FER topological structure, the octatomic ring for possessing ten-ring duct (4.2 × 5.4) and intersecting Duct (3.5 × 4.8), at the same the hexatomic ring duct parallel with ten-ring duct and octatomic ring duct be crossed to form one it is ellipse Spherical small cage, referred to as " ferrierite cage ".ZSM-5 molecular sieve have MFI topological structure, possess ten-ring straight hole road (5.3 × 5.6) with the Z-shaped duct of ten-ring (5.1 × 5.5), duct intersects to form three dimensional intersection cellular structure.ZSM-35 molecular sieve and ZSM-5 molecular sieve belongs to ten-ring cellular structure molecular sieve, respectively in methanol-to-olefins, catalytic cracking, olefin cracking, isomery Unique catalytic performance is shown in the reaction such as change, and since there are many Spatial Dimensions of multiplicity and connection for ten-ring molecular sieve Type, each molecular sieve show different catalytic characteristics again in same reaction.Therefore, compound point of ZSM-35/ZSM-5 is developed Son sieve will combine the advantage of ZSM-35 molecular sieve and ZSM-5 molecular sieve, in the reaction process such as olefin cracking and methanol-to-olefins Show unique catalytic.Currently, not there is the open report of ZSM-35/ZSM-5 composite molecular screen.
Summary of the invention
The purpose of the present invention is to propose to a kind of ZSM-35/ZSM-5 composite molecular screen, which has FER simultaneously The structure feature of topological structure and MFI topological structure molecular sieve generates ZSM-35 molecular sieve but also guiding life using that can be oriented to It is template at the isopropylamine of ZSM-5 molecular sieve, ZSM-35/ZSM-5 composite molecular screen is prepared in hydrothermal synthesis.What is obtained answers Conjunction molecular sieve structure is stable, composition is controllable, has excellent performance.Preparation method step is simple and convenient to operate, and is easy to industrial applications.
Realize the specific technical solution of the object of the invention:
A kind of ZSM-35/ZSM-5 composite molecular screen, feature are that the molecular sieve has ZSM-35 molecular sieve and ZSM-5 molecular sieve Structure feature, wherein ZSM-35 molecular sieve accounts for the 5 ~ 95% of composite molecular screen composition;The preparation method of the composite molecular screen, including Step in detail below:
The preparation of first step reaction mixture
By the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water 1:(0.015 ~ 0.1 in molar ratio): (0.15 ~ 0.23): (0.1 ~ 1.0): (10 ~ 50) be uniformly mixed, prepare reaction mixture, wherein the silicon source be silica solution, At least one of silica gel and waterglass, the silicon source are at least one of sodium metaaluminate, aluminum sulfate and aluminum nitrate, described Alkali source be NaOH, the template is isopropylamine;
Second step hydro-thermal process
It will be transferred in closed reactor through reaction mixture made from upper step, it is small in 150~190 DEG C of hydro-thermal process 24~72 When, the ZSM-35/ZSM-5 composite molecular screen is obtained after being then filtered, washed, dried, being roasted.
Compared with existing technology, the present invention has following remarkable advantage:
1, there is not ZSM-35/ZSM-5 composite molecular screen at present, which has expanded compound point containing ZSM-35 molecular sieve The type of son sieve.
2, ZSM-35/ZSM-5 composite molecular screen stable structure, composition are controllable.
3, synthesis process is simple, easy to operate, easy to industrialized production.
Detailed description of the invention
Fig. 1 is the XRD spectra of ZSM-35/ZSM-5 composite molecular screen, ZSM-35 molecular sieve and ZSM-5 molecular sieve;
Fig. 2 is the electromicroscopic photograph figure for the ZSM-35/ZSM-5 composite molecular screen that embodiment 1 is prepared.
Specific embodiment
The operating procedure of all embodiments according to the above technical scheme is operated.
Embodiment 1
The preparation of first step reaction mixture
By the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water 1:0.05:0.18 in molar ratio: 0.6:20 is uniformly mixed, and prepares reaction mixture, wherein it is sodium metaaluminate that the silicon source, which is silica solution, the silicon source, institute The alkali source stated is NaOH, and the template is isopropylamine;
Second step hydro-thermal process
To be transferred in closed reactor through reaction mixture made from upper step, in 170 DEG C hydro-thermal process 72 hours, then pass through The ZSM-35/ZSM-5 composite molecular screen is obtained after filter, washing, dry, roasting.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is as shown in figure 1 shown in A, and wherein ZSM-35 molecular sieve accounts for multiple Close the 72% of molecular sieve.
The XRD spectra from Fig. 1 is it is found that ZSM-35/ZSM-5 composite molecular screen has ZSM-35 molecular sieve and ZSM-5 simultaneously The structure feature of molecular sieve;The stereoscan photograph from Fig. 2 it is found that ZSM-35/ZSM-5 composite molecular screen by biggish sheet ZSM-35 molecular sieve and lesser fine particle ZSM-5 molecular sieve intertexture symbiosis are formed.
Embodiment 2
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.24:0.6:20 is uniformly mixed, and prepares reaction mixture.
It obtains in the XRD spectra and Fig. 1 of product ZSM-35 molecular sieve shown in B, is pure phase FER topological structure molecular sieve.
Embodiment 3
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.14:0.6:20 is uniformly mixed, and prepares reaction mixture.
It obtains in the XRD spectra and Fig. 1 of product ZSM-5 molecular sieve shown in C, is pure phase MFI topological structure molecular sieve.
Embodiment 4
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.16:0.8:50 is uniformly mixed, and prepares reaction mixture.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for multiple Close the 33% of molecular sieve.
Embodiment 5
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.20:1.0:50 is uniformly mixed, and prepares reaction mixture.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for multiple Close the 89% of molecular sieve.
Embodiment 6
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.23:0.5:15 is uniformly mixed, and prepares reaction mixture.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for multiple Close the 93% of molecular sieve.
Embodiment 7
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.22:0.6:20 is uniformly mixed, and prepares reaction mixture, and the silicon source is the sodium metaaluminate for being 7:3 according to weight ratio With the mixture of aluminum sulfate.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for multiple Close the 90% of molecular sieve.
Embodiment 8
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.16:0.3:25 is uniformly mixed, and prepares reaction mixture.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for multiple Close the 15% of molecular sieve.
Embodiment 9
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.15:0.6:20 is uniformly mixed, and prepares reaction mixture.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for multiple Close the 8% of molecular sieve.
Embodiment 10
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.025:0.18:0.6:20 is uniformly mixed, and prepares reaction mixture;
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for compound point The 68% of son sieve.
Embodiment 11
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.025:0.18:0.5:30 is uniformly mixed, and prepares reaction mixture;Second step in 190 DEG C hydro-thermal process 24 hours
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for compound point The 68% of son sieve.
Embodiment 12
Except for the following differences, remaining is with embodiment 1 for implementation process:
In the first step by the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water in molar ratio 1: 0.05:0.20:0.6:20 is uniformly mixed, and prepares reaction mixture, and the silicon source is the silica solution and silicon for being 8:2 according to weight ratio Glue mixture;Second step in 150 DEG C hydro-thermal process 36 hours.
The XRD spectra of product ZSM-35/ZSM-5 composite molecular screen is similar with A in Fig. 1, and wherein ZSM-35 molecular sieve accounts for multiple Close the 85% of molecular sieve.

Claims (3)

1. a kind of preparation method of ZSM-35/ZSM-5 composite molecular screen, it is characterised in that this method comprising the following specific steps
The preparation of first step reaction mixture
By the SiO in silicon source2, Al in silicon source2O3, OH in alkali source-, template and water 1:(0.015 ~ 0.1 in molar ratio): (0.15 ~ 0.23): (0.1 ~ 1.0): (10 ~ 50) be uniformly mixed, prepare reaction mixture, wherein the silicon source be silica solution, At least one of silica gel and waterglass, the silicon source are at least one of sodium metaaluminate, aluminum sulfate and aluminum nitrate, described Alkali source be NaOH, the template is isopropylamine;
Second step hydro-thermal process
It will be transferred in closed reactor through reaction mixture made from the first step, it is small in 150~190 DEG C of hydro-thermal process 24~72 When, the ZSM-35/ZSM-5 composite molecular screen is obtained after being then filtered, washed, dried, being roasted.
2. ZSM-35/ZSM-5 composite molecular screen made from a kind of claim 1 the method.
3. ZSM-35/ZSM-5 composite molecular screen according to claim 2, which is characterized in that the molecular sieve has ZSM-35 The structure feature of molecular sieve and ZSM-5 molecular sieve, wherein ZSM-35 molecular sieve accounts for the 5 ~ 95% of composite molecular screen composition.
CN201910449975.5A 2019-05-28 2019-05-28 A kind of ZSM-35/ZSM-5 composite molecular screen and preparation method thereof Pending CN110127718A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112619698A (en) * 2019-09-24 2021-04-09 中国石油化工股份有限公司 ZSM-5/ZSM-35 composite molecular sieve and preparation method thereof

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US20040138051A1 (en) * 1999-09-07 2004-07-15 Zhiping Shan Novel zeolite composite, method for making and catalytic application thereof
CN1504409A (en) * 2002-11-29 2004-06-16 中国石油天然气股份有限公司 ZSM-35/MCM-22 cocrystallization molecular sieve and preparation method thereof
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112619698A (en) * 2019-09-24 2021-04-09 中国石油化工股份有限公司 ZSM-5/ZSM-35 composite molecular sieve and preparation method thereof
CN112619698B (en) * 2019-09-24 2023-03-10 中国石油化工股份有限公司 ZSM-5/ZSM-35 composite molecular sieve and preparation method thereof

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Application publication date: 20190816