CN111732110A - NaY zeolite and preparation method thereof - Google Patents

NaY zeolite and preparation method thereof Download PDF

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CN111732110A
CN111732110A CN202010070691.8A CN202010070691A CN111732110A CN 111732110 A CN111732110 A CN 111732110A CN 202010070691 A CN202010070691 A CN 202010070691A CN 111732110 A CN111732110 A CN 111732110A
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nay zeolite
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zeolite
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CN111732110B (en
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申宝剑
刘鹏
聂锁府
郭巧霞
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China University of Petroleum Beijing
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    • 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
    • C01B39/20Faujasite type, e.g. type X or Y
    • C01B39/24Type Y
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y40/00Manufacture or treatment of nanostructures
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    • 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
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    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
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    • C01P2004/60Particles characterised by their size
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    • C01P2004/60Particles characterised by their size
    • C01P2004/64Nanometer sized, i.e. from 1-100 nanometer

Abstract

The invention provides NaY zeolite and a preparation method thereof, wherein the preparation method of the NaY zeolite comprises the following steps of (4.6 × 10)‑7‑2.0×10‑4) Polyacrylamide (10-30) Na2O:Al2O3:(10‑30)SiO2:(150‑450)H2Mixing a silicon source, an aluminum source, polyacrylamide and water according to the molar ratio of O to prepare a guiding agent; according to (1-4) Na2O:Al2O3:(7‑10)SiO2:(100‑300)H2Mixing a guiding agent, a silicon source, an alkali source, an aluminum source and water according to the molar ratio of O to prepare reaction mixture gel, wherein the guiding agent accounts for 5-15% of the total mass of the reaction mixture gel as 100%; and carrying out crystallization reaction on the prepared reaction mixture gel to obtain the NaY zeolite. The preparation method can prepare high crystallinityFlaky and small-grained NaY zeolite.

Description

NaY zeolite and preparation method thereof
Technical Field
The invention belongs to the field of inorganic materials and catalysts, and particularly relates to NaY zeolite and a preparation method thereof.
Background
The Y zeolite has developed three-dimensional pore passages, adjustable acidity, good thermal stability and good hydrothermal stability, and is widely applied to the petroleum refining industry. Degree of crystallinity, silicon to aluminum ratio (SiO)2/Al2O3) And the grain size are the most important factors influencing the properties and functions of the Y-type zeolite. When applied to catalytic cracking, higher crystal retention means more active centers and higher catalytic performance; the ratio of the framework silicon to the aluminum is properly improved, so that the reduction of the density of acid centers is facilitated, the acid strength is improved, and bimolecular hydrogen transfer reactions in catalytic cracking can be reduced, so that the method has the advantages of good coke selectivity and improved octane number, and has higher thermal stability and hydrothermal stability; the smaller grain size enables the zeolite to expose more active sites, is more beneficial to the conversion of heavy oil macromolecules, is also more beneficial to the diffusion of product molecules, and reduces the secondary cracking of intermediate useful products and the generation of coke.
NaY zeolite is the largest molecular sieve catalytic material, and is used as the main raw material for producing ultrastable Y zeolite (USY molecular sieve), and its performance directly affects the performance of USY molecular sieve, and further affects the performance of catalyst. The improvement of the property of the NaY zeolite not only can improve the stability of the active component USY molecular sieve of the catalytic cracking catalyst in the production process and improve the operation flexibility of the production, but also can improve the crystallinity, the pore structure property and the like of the USY molecular sieve, and has important significance for improving the property of the catalyst and expanding the competitiveness of catalyst services.
At present, the method for industrially producing NaY molecular sieves mostly adopts a guide agent method similar to those proposed by Grace company in US3639099 and US3671191, and NaY molecular sieve products with the crystallinity of more than 83 percent and the silicon-aluminum of about 5.0 can be synthesized by the method within 28 hours, but the crystallinity of more than 90 percent is difficult. In addition, the conventional grain size Y-type zeolite with the grain size of more than 500nm is prepared by the prior art. However, with the heavy oil product, the macromolecular reactant is difficult to diffuse into the crystal and further difficult to contact with the active site, so that the conventional grain size Y-type zeolite cannot meet the requirement of high-efficiency heavy oil conversion, and therefore, the preparation of small-grain Y-type zeolite becomes a focus of attention.
The small-grain Y-type zeolite has the advantages of higher specific surface area, shorter diffusion path, more easily-contacted active sites and the like, is favored by researchers, and has the effect equivalent to that of mesoporous Y-type zeolite. CN105314651A discloses a method for synthesizing small-grain Y-type zeolite, which adopts hexamethylenetetramine as an additive and obtains the small-grain Y-type zeolite with the grain size of 400-600nm through fractional crystallization, but the crystallinity is lower. CN1113814C adopts organic dispersant glycerol, ethylene glycol or isopropanol to prepare the small-grain Y-type zeolite with the grain size of 300-600 nm. There are also some methods of preparing small-grained Y-type zeolite (CN101007639B) having a size of 300nm or less using inorganic additives (pseudo-boehmite, alpha-gibbsite and beta-gibbsite), but having low crystallinity and low specific surface area. Although the nano Y-type zeolite is successfully prepared by CN104843738A, CN106698460A and CN106672996A, expensive organic additives or fluorine-containing compounds are used, and the dosage is high, which is not beneficial to industrial application and environmental protection. As for the research results at present, no mature method for synthesizing the small-grain (100-. In addition, in the synthesis process of ZSM-5 zeolite, a single small-molecule organic template (3, 5-dimethyl-N-butyl pyridine iodide) is provided for inhibiting the growth of a B axis of a ZSM-5 molecular sieve, so that the method (CN106587100B) for preparing the flaky ZSM-5 zeolite is provided, and the diffusion capacity of product molecules in the B axis direction is greatly improved.
If the advantages of the small-grained zeolite and the flaky zeolite are combined and are introduced into the preparation of the Y-type zeolite, the method is a breakthrough research result. Therefore, the research and development of the effective small-grain Y-type zeolite which is suitable for industrial production and has the nano-sheet structure has important significance for the field of zeolite catalysis.
Disclosure of Invention
The invention aims to provide a preparation method of NaY zeolite. The preparation method can synthesize the NaY zeolite with high crystallinity, sheet shape and small crystal grain in a short time.
In order to achieve the above object, the present invention provides a method for preparing NaY zeolite, wherein the method comprises:
1) preparation of directing agent according to (4.6 × 10)-7-2.0×10-4) Polyacrylamide (10-30) Na2O:Al2O3:(10-30)SiO2:(150-450)H2Mixing a silicon source, an aluminum source, polyacrylamide and water according to the molar ratio of O to prepare a guiding agent;
2) preparation of reaction mixture gel: according to (1-4) Na2O:Al2O3:(7-10)SiO2:(100-300)H2Mixing a guiding agent, a silicon source, an alkali source, an aluminum source and water according to the molar ratio of O to prepare reaction mixture gel; wherein, the amount of the guiding agent accounts for 5 to 15 percent based on the total mass of the reaction mixture gel as 100 percent;
3) gel crystallization of the reaction mixture: and 2) carrying out crystallization reaction on the reaction mixture gel prepared in the step 2) to prepare the NaY zeolite.
In the above method for preparing NaY zeolite, preferably, the silicon source includes at least one of water glass, silica sol, white carbon black and sodium silicate; in a preferred embodiment, the silicon source is water glass.
In the above method for preparing NaY zeolite, preferably, the aluminum source comprises at least one of sodium metaaluminate, high alkali sodium metaaluminate, aluminum sulfate and aluminum nitrate; in a preferred embodiment, the aluminum source is selected from high alkali sodium metaaluminate.
In the above method for preparing NaY zeolite, preferably, the alkali source comprises at least one of sodium metaaluminate, high alkali sodium metaaluminate, sodium hydroxide and potassium hydroxide; in a preferred embodiment, the aluminum source is selected from high alkali sodium metaaluminate.
In the method for preparing NaY zeolite, the polyacrylamide may be at least one selected from the group consisting of nonionic, cationic, anionic and amphoteric.
In the preparation method of the NaY zeolite, preferably, the silicon source, the aluminum source, the polyacrylamide and the water are mixed in the step 1), and then aged for 4-60 hours at 10-50 ℃ to prepare the directing agent.
In a specific embodiment, the silicon source, the aluminum source and the water are mixed, then the polyacrylamide is added, the mixture is stirred and mixed uniformly at the temperature of 10-50 ℃, and then the mixture is aged for 4-60 hours at the temperature of 10-50 ℃ to prepare the guiding agent.
In the preparation method of the NaY zeolite, the preparation mode of the directing agent can adopt both dynamic and static states.
In the above method for preparing NaY zeolite, preferably, the preparation of the reaction mixture gel is performed at 30 to 70 ℃.
In the above method for preparing NaY zeolite, preferably, the step 2) of mixing the directing agent, the silicon source, the alkali source, the aluminum source and the water comprises: firstly, mixing a guiding agent and a silicon source, and then adding an alkali source, an aluminum source and water to prepare reaction mixture gel; more preferably, the alkali source is added first and then the aluminum source. The guiding agent is mixed with the silicon source before the alkali source and the aluminum source are added, so that the guiding agent is favorably dispersed in the silicon source, and the interaction of polyacrylamide with the silicon source and the aluminum source is promoted. And an aluminum source is added after the alkali source is added, so that the good dispersion of the guiding agent in the silicon source is facilitated, and the interaction of the polyacrylamide with the silicon source and the aluminum source is further promoted.
In the preparation method of the NaY zeolite, the guiding agent and the silicon source are mixed, and the method can be realized by adding the guiding agent into the silicon source or adding the silicon source into the guiding agent.
In a specific embodiment, the guiding agent and the silicon source are mixed and stirred for 1-90 h; then adding an alkali source, an aluminum source and water, and stirring for 1-24h to prepare reaction mixture gel.
In the above method for preparing NaY zeolite, preferably, the temperature of the crystallization reaction in step 3) is 70 to 100 ℃.
In the above method for preparing NaY zeolite, preferably, the time of the crystallization reaction in step 3) is 6 to 50 hours.
In the above method for preparing NaY zeolite, preferably, the flaky small-grained NaY zeolite is obtained by filtering, washing and drying after the crystallization reaction in step 3).
In the preparation method of the NaY zeolite, the crystallization mode can adopt dynamic crystallization or static crystallization.
The invention also provides NaY zeolite prepared by the preparation method of the NaY zeolite, wherein the crystallinity of the NaY zeolite is more than 90 percent, and the SiO zeolite has the mole ratio of silicon to aluminum2/Al2O34.5-5.9, crystal grain size below 300nm, and nano-flake NaY zeolite with nano-flake thickness of 50-100 nm.
Among the above NaY zeolites, it is preferable that the NaY zeolite has a specific surface area of 700m2More than g, and the mesoporous volume is 0.101-0.150cm3Per g, pore volume 0.440cm3More than g.
In the above NaY zeolite, preferably, the NaY zeolite has a crystal grain size of 75 to 300 nm.
In the NaY zeolite, the amount of the nano-flake NaY zeolite is preferably 10% to 60% based on 100% of the number of crystal grains of the NaY zeolite.
The preparation method of the NaY zeolite provided by the invention adopts a guiding agent added with polyacrylamide to prepare reactant gel, and the reactant gel is crystallized to obtain the NaY zeolite with high crystallinity, nano-flake shape and small crystal grains. Compared with the prior art, the technical scheme provided by the invention has the following advantages:
1. the preparation method of the NaY zeolite provided by the invention can synthesize the crystallinity of more than 90% (even more than 95%) and the silicon-aluminum molar ratio (SiO) in relatively short time (such as 6-50h) with relatively low alkalinity and relatively low feeding silicon-aluminum ratio2/Al2O3) NaY zeolite of 4.5-5.9, and the NaY zeolite contains partial nano-sheet NaY zeolite.
2. The NaY zeolite prepared by the preparation method of the NaY zeolite provided by the invention is small-grained NaY zeolite with the grain size of below 300nm (usually 75-300nm) and in a nanometer scale, and contains part of nano flaky NaY zeolite (usually 10% -60% of nano flaky NaY zeolite).
3. Na provided by the inventionThe NaY zeolite prepared by the preparation method of the Y zeolite has a better pore structure and a larger specific surface area (generally reaching 700 m)2More than g), a relatively large pore volume (typically up to 0.440 cm)3More than g), larger mesoporous volume (usually reaching 0.101-0.150 cm)3/g)。
4. The preparation method of NaY zeolite provided by the invention can be used for the existing industrial NaY zeolite production device, does not need to add other equipment, has better industrialization prospect, and has very important significance for improving the performance of the catalytic cracking catalyst.
5. The preparation method of the NaY zeolite provided by the invention has the advantages of small material dosage, low cost, high utilization rate, capability of realizing rapid preparation and simple process.
6. According to the preparation method of the NaY zeolite, the organic additive (polyacrylamide) is less in material feeding in the preparation process and wide in available types (including nonionic type, anionic type, cationic type and amphoteric type), the guiding agent added with the polyacrylamide can be prepared at a relatively mild temperature within a relatively short time, the preparation method provided by the invention can realize the completion of crystallization within a relatively short time, and compared with the conventional preparation method of the NaY zeolite, the preparation method has the advantages of energy consumption reduction and good industrial prospect.
Drawings
Figure 1A is an XRD pattern of the NaY zeolite provided in example 1.
Figure 1B is an XRD pattern of the NaY zeolite provided in comparative example 1.
Figure 1C is an XRD pattern of the NaY zeolite provided in comparative example 2.
Figure 1D is an XRD pattern of the NaY zeolite provided in comparative example 3.
Figure 2A is an SEM image of the NaY zeolite provided in example 1.
Fig. 2B is an SEM image of the NaY zeolite provided in comparative example 1.
Fig. 2C is an SEM image of the NaY zeolite provided in comparative example 2.
Figure 2D is an SEM image of the NaY zeolite provided in comparative example 3.
FIG. 3 shows example 1 and comparative example1. Comparative example 3, N of NaY zeolite provided in comparative example 32Physical adsorption desorption curve.
Detailed Description
The technical solutions of the present invention will be described in detail below in order to clearly understand the technical features, objects, and advantages of the present invention, but the present invention is not limited to the practical scope of the present invention.
In the examples and comparative examples according to the invention, the relative crystallinity and the silica-alumina ratio of the NaY zeolite synthesized were determined using an X-ray diffractometer model BRUKER D8 ADVANCE (BRUKER, germany) under the following experimental conditions: CuKa radiation (0.1541nm), tube voltage 40kV, and tube current 40 mA. The relative crystallinity was determined according to SH/T0340-92 standard method (Association for chemical industry standards), published by the national standards Press, 2000. The silica-alumina ratio was determined according to the SH/T0339-92 standard method (edited in the chemical industry standards, published by the Chinese Standard Press, 2000), and the unit cell constant of NaY zeolite was calculated according to the formula (1) and then the ratio was determined according to the formula Breck-Flanigen: calculated as Si/Al (25.858- α)/(α -24.191).
Figure BDA0002377221690000051
Wherein, A is a unit cell constant,
Figure BDA0002377221690000052
lambda is CuK α1Wavelength of radiation
Figure BDA0002377221690000053
h2+k2+l2Is the X-ray diffraction miller index sum of squares.
Zeolite standards used in examples and comparative examples as standards for crystallinity used in crystalline examples and comparative examples were obtained from the industrial NaY reference sample No. 040617, and the SiO of the zeolite was measured by X-ray diffraction2/Al2O3Was 5.1, and its crystallinity was set to 100%.
In each of the examples and comparative examples, the synthesized NaY zeolite had a morphology and a crystal grain size using a ZEISS GeminiSEM model 300 (ZEISS, germany) thermal field emission scanning electron microscope with an acceleration voltage of 20kV to 30kV, a resolution limit of about 1.2nm, and a magnification of 25K to 200K.
In each of the examples and comparative examples, the pore structure of the synthesized NaY zeolite was measured using a U.S. micromeritics tristar 3020 physical adsorption apparatus. Calculating the specific surface area of the sample by a BET formula, obtaining a pore size distribution curve by adopting a BJH method from an isothermal adsorption curve, calculating the specific surface area and the pore volume of micropores by using a t-plot method, and obtaining the total pore volume of the sample when the relative pressure is 0.9944.
Example 1
This example provides a preparation method of NaY zeolite, which includes:
33.1g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), 25.5g of high-alkali sodium metaaluminate solution (Al) prepared from alkali solution and sodium metaaluminate2O33.16 wt% of Na2The content of O is 21.11wt percent), 2g of nonionic polyacrylamide (with molecular weight of 400 ten thousand and hydrolysis degree of 30 percent) and 15g of water are uniformly mixed, stirred uniformly at 34 ℃, and statically aged for 18 hours to prepare a guiding agent;
130g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing into a beaker placed in a water bath at 40 deg.C, adding the above guiding agent under stirring, stirring for 1 hr, and adding 40.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt% of O and 60g of water, stirring for 0.5h, and adding 99.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) filling the reaction mixture gel into a reaction kettle, statically crystallizing for 16 hours at the temperature of 98 ℃, and then filtering, washing and drying to obtain the NaY zeolite.
The XRD characterization of the NaY zeolite prepared in this example is shown in fig. 1A, the SEM figure is shown in fig. 2A (for characterizing the crystal morphology and the grain size), the physisorption desorption isotherm is shown in fig. 3, the silica-alumina ratio and the crystallinity are shown in table 1, and the structural properties are shown in table 2.
The crystal of the NaY zeolite prepared by the embodiment is in the shape of faujasite, the grain size is 200-300nm, wherein part of the crystal is in the shape of nano-sheet, and the thickness of the nano-sheet NaY zeolite is 20-50 nm; the amount of the nano flaky NaY zeolite accounts for 43 percent based on the number of the crystal grains of the NaY zeolite as 100 percent.
Example 2
This example provides a preparation method of NaY zeolite, which includes:
33.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 25.5g of high alkali sodium metaaluminate (Al) were added2O33.16 wt% of Na2The content of O is 21.11wt percent), 2g of cationic polyacrylamide (the molecular weight is 700 ten thousand, the hydrolysis degree is about 37 percent) and 15g of water are uniformly mixed, stirred uniformly at 34 ℃, and statically aged for 18 hours to prepare a guiding agent;
130g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing into a beaker placed in a water bath at 40 deg.C, adding the above guiding agent under stirring, stirring for 1 hr, and adding 40.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt% of O and 60g of water, stirring for 0.5h, and adding 99.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) filling the reaction mixture gel into a reaction kettle, statically crystallizing for 20 hours at the temperature of 98 ℃, and then filtering, washing and drying to obtain the NaY zeolite.
The NaY zeolite prepared in this example had a relative crystallinity of 95% and a silicon to aluminum ratio (SiO)2/Al2O3) Is 5.10, and has a specific surface area of 722m2Per g, pore volume 0.410cm3(g) the mesoporous volume is 0.108cm3(ii) in terms of/g. The crystal is in the shape of faujasite, the grain size is 200-300nm, the shape of part of the crystal is in the shape of nano-sheet, and the thickness of the nano-sheet NaY zeolite is 20-50 nm; the amount of the nano flaky NaY zeolite accounts for 100 percent of the crystal grain number of the NaY zeolite35%。
Example 3
This example provides a preparation method of NaY zeolite, which includes:
33.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 25.5g of high alkali sodium metaaluminate (Al) were added2O33.16 wt% of Na2The content of O is 21.11wt percent), 2g of anionic polyacrylamide (the molecular weight is 700 ten thousand, the hydrolysis degree is about 35 percent) and 15g of water are evenly mixed, evenly stirred at 40 ℃ and dynamically aged for 12 hours to prepare a guiding agent;
130g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing in a beaker placed in a water bath at 60 deg.C, adding the above guiding agent under stirring, stirring for 1 hr, and adding 40.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt% of O and 60g of water, stirring for 2 hours, and then adding 99.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) putting the reaction mixture gel into a reaction kettle, statically crystallizing at 96 ℃ for 24 hours, and then filtering, washing and drying to obtain the NaY zeolite.
The NaY zeolite prepared in this example had a relative crystallinity of 94% and a silicon to aluminum ratio (SiO)2/Al2O3) Is 5.05, and the specific surface area is 712m2Per g, pore volume 0.416cm3(g) mesoporous volume is 0.111cm3(ii) in terms of/g. The crystal is in the shape of faujasite, the grain size is 200-300nm, the shape of part of the crystal is in the shape of nano-sheet, and the thickness of the nano-sheet NaY zeolite is 20-50 nm; the amount of the nano flaky NaY zeolite accounts for 40 percent based on the number of the crystal grains of the NaY zeolite as 100 percent.
Example 4
This example provides a preparation method of NaY zeolite, which includes:
35.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 28.5g of high alkali sodium metaaluminate (Al)2O33.16 wt% of Na2The O content is 21.11wt percent), 5g of amphoteric polyacrylamide (molecular weight is 200 ten thousand, the hydrolysis degree is about 27 percent, Chengdu Aike reagent, model No. 9003-05-8) and 20g of water are uniformly mixed, stirred uniformly at 25 ℃, dynamically aged for 24 hours, and prepared into a guiding agent;
110.6g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing into a beaker placed in a water bath at 50 deg.C, adding the above directing agent under stirring, and adding 44.9g of high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt% of O and 50.6g of water, stirring for 2 hours, and then adding 83.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) filling the reaction mixture gel into a reaction kettle, statically crystallizing at 90 ℃ for 32 hours, and then filtering, washing and drying to obtain the NaY zeolite.
The NaY zeolite prepared in this example had a relative crystallinity of 97% and a silicon to aluminum ratio (SiO)2/Al2O3) Is 5.15, and has a specific surface area of 726m2Per g, pore volume 0.426cm3(g) mesoporous volume is 0.125cm3(ii) in terms of/g. The crystal is in the shape of faujasite, the grain size is 200-300nm, the shape of part of the crystal is in the shape of nano-sheet, and the thickness of the nano-sheet NaY zeolite is 20-50 nm; the amount of the nano flaky NaY zeolite accounts for 45 percent based on the number of the crystal grains of the NaY zeolite as 100 percent.
Example 5
This example provides a preparation method of NaY zeolite, which includes:
33.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 25.5g of high alkali sodium metaaluminate (Al) were added2O33.16 wt% of Na2The content of O is 21.11wt percent), 3g of cationic polyacrylamide (the molecular weight is 700 ten thousand, the hydrolysis degree is about 37 percent) and 15g of water are uniformly mixed, stirred uniformly at 40 ℃, and statically aged for 16 hours to prepare a guiding agent;
110.5g of water glass (SiO)2The content is 27.6wt%,Na2O content of 8.96 wt%), placing in a beaker placed in a water bath at 40 deg.C, adding the above guiding agent under stirring, stirring for 5 hr, and adding 45.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt.% of O and 50.8g of water, stirred for 1 hour and then added with 79.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) filling the reaction mixture gel into a reaction kettle, statically crystallizing for 30 hours at 96 ℃, and then filtering, washing and drying to obtain the NaY zeolite.
The NaY zeolite prepared in this example had a relative crystallinity of 98% and a silicon to aluminum ratio (SiO)2/Al2O3) Is 5.13, and has a specific surface area of 716m2Per g, pore volume 0.417cm3(g) mesoporous volume is 0.112cm3(ii) in terms of/g. The crystal is in the shape of faujasite, the grain size is 200-300nm, the shape of part of the crystal is in the shape of nano-sheet, and the thickness of the nano-sheet NaY zeolite is 20-50 nm; the amount of the nano flaky NaY zeolite accounts for 51 percent based on the number of the crystal grains of the NaY zeolite as 100 percent.
Example 6
This example provides a preparation method of NaY zeolite, which includes:
33.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 25.5g of high alkali sodium metaaluminate (Al) were added2O33.16 wt% of Na2The content of O is 21.11wt percent), 1g of cationic polyacrylamide (the molecular weight is 700 ten thousand, the hydrolysis degree is about 37 percent) and 15g of water are uniformly mixed, stirred uniformly at 34 ℃, and statically aged for 18 hours to prepare a guiding agent;
130g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing into a beaker placed in a water bath at 40 deg.C, adding the above guiding agent under stirring, stirring for 1 hr, and adding 40.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt% of O and 60g of water, stirring for 0.5h, and adding 99.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 6 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) filling the reaction mixture gel into a reaction kettle, statically crystallizing for 16 hours at the temperature of 98 ℃, and then filtering, washing and drying to obtain the NaY zeolite.
The NaY zeolite prepared in this example had a relative crystallinity of 98% and a silicon to aluminum ratio (SiO)2/Al2O3) Is 5.14, and has a specific surface area of 720m2Per g, pore volume 0.427cm3(g) the mesoporous volume is 0.109cm3(ii) in terms of/g. The crystal is in the shape of faujasite, the grain size is 200-300nm, the shape of part of the crystal is in the shape of nano-sheet, and the thickness of the nano-sheet NaY zeolite is 20-50 nm; the amount of the nano flaky NaY zeolite accounts for 48 percent based on the number of the crystal grains of the NaY zeolite as 100 percent.
Comparative example 1
This comparative example provides a method of preparing NaY zeolite (without addition of polyacrylamide), comprising:
33.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 25.5g of high alkali sodium metaaluminate (Al) were added2O33.16 wt% of Na2The O content is 21.11wt percent) and 15g of water are evenly mixed, evenly stirred at 34 ℃, and statically aged for 18 hours to prepare a guiding agent;
130g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing into a beaker placed in a water bath at 40 deg.C, adding the above guiding agent under stirring, stirring for 1 hr, and adding 40.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt% of O and 60g of water, stirring for 0.5h, and adding 99.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) filling the reaction mixture gel into a reaction kettle, statically crystallizing for 46h at the temperature of 98 ℃, and then filtering, washing and drying to obtain the NaY zeolite.
The XRD characterization of the NaY zeolite prepared in this comparative example is shown in fig. 1B, the SEM figure is shown in fig. 2B (for characterizing the crystal morphology and the grain size), the physisorption desorption isotherm is shown in fig. 3, the silica-alumina ratio and the crystallinity are shown in table 1, and the structural properties are shown in table 2.
The crystal of the NaY zeolite prepared by the embodiment is in the shape of faujasite, the grain size is 500-600nm, and the nano flaky NaY zeolite does not appear.
Comparative example 2
This comparative example provides a method for preparing NaY zeolite, which differs from example 1 only in that: the polyacrylamide is added in the preparation process of the gel, the other steps are the same as the example 1, and the preparation method specifically comprises the following steps:
33.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 25.5g of high alkali sodium metaaluminate (Al) were added2O33.16 wt% of Na2The O content is 21.11wt percent) and 15g of water are evenly mixed, evenly stirred at 34 ℃, and statically aged for 18 hours to prepare a guiding agent;
130g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing into a beaker placed in a water bath at 40 deg.C, adding the above guiding agent under stirring, stirring for 1 hr, and adding 40.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 percent of O content and 60g of water, 2g of nonionic polyacrylamide (molecular weight of 400 ten thousand and hydrolysis degree of 30 percent) is added, and after stirring for 0.5h, 99.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) filling the reaction mixture gel into a reaction kettle, statically crystallizing for 16 hours at the temperature of 98 ℃, and then filtering, washing and drying to obtain the NaY zeolite.
The XRD characterization of the NaY zeolite prepared in this comparative example is shown in fig. 1C, the SEM figure is shown in fig. 2C (for characterizing the crystal morphology and the grain size), the physisorption desorption isotherm is shown in fig. 3, the silica-alumina ratio and the crystallinity are shown in table 1, and the structural properties are shown in table 2.
The crystal of the NaY zeolite prepared by the embodiment has the oval crystal morphology of P-type zeolite, the grain size is about 300nm, and the nano flaky NaY zeolite does not appear.
Comparative example 3
This comparative example provides a method for preparing NaY zeolite, which differs from example 1 only in that: the polyacrylamide is added in the crystallization process, the other steps are the same as the example 1, and the preparation method specifically comprises the following steps:
33.1g of water glass (SiO)227.6 wt% of Na2O content 8.96 wt%), 25.5g of high alkali sodium metaaluminate (Al) were added2O33.16 wt% of Na2The O content is 21.11wt percent) and 15g of water are evenly mixed, evenly stirred at 34 ℃, and statically aged for 18 hours to prepare a guiding agent;
130g of water glass (SiO)227.6 wt% of Na2O content of 8.96 wt%), placing into a beaker placed in a water bath at 40 deg.C, adding the above guiding agent under stirring, stirring for 1 hr, and adding 40.9g high-alkali sodium metaaluminate (Al)2O33.16 wt% of Na221.11 wt% of O and 60g of water, stirring for 0.5h, and adding 99.2g of aluminum sulfate (Al)2O3Content 7.6 wt%) was stirred for 3 hours and mixed uniformly to obtain a reaction mixture gel;
and (3) placing the reaction mixture gel and 2g of nonionic polyacrylamide (with the molecular weight of 400 ten thousand and the degree of hydrolysis of 30%) into a reaction kettle, carrying out static crystallization for 16 hours at 98 ℃, and filtering, washing and drying after the static crystallization is finished to obtain the NaY zeolite.
The XRD characterization of the NaY zeolite prepared in this comparative example is shown in fig. 1D, the SEM figure is shown in fig. 2D (for characterizing the crystal morphology and the grain size), the physisorption desorption isotherm is shown in fig. 3, the silica-alumina ratio and the crystallinity are shown in table 1, and the structural properties are shown in table 2.
The crystal of the NaY zeolite prepared in this example is basically the crystal morphology of faujasite, but the crystal morphology is irregular, the grain size is about 500nm, and no nano-flaky NaY zeolite appears.
TABLE 1
Figure BDA0002377221690000121
TABLE 2
Figure BDA0002377221690000122
Wherein S isBETIs the total specific surface area, SMicroIs the specific surface area of the micropores, SExternalIs an external specific surface area, VTotallIs the total pore volume, VMicroIs a micropore volume, VMesoIs the mesoporous volume.
Although the present invention has been described in detail with reference to the above embodiments, it should be understood by those skilled in the art that: modifications and equivalents may be made thereto without departing from the spirit and scope of the invention and it is intended to cover any modifications or equivalents as may fall within the scope of the invention.

Claims (10)

1. A method for preparing NaY zeolite, wherein the method comprises:
1) preparation of directing agent according to (4.6 × 10)-7-2.0×10-4) Polyacrylamide (10-30) Na2O:Al2O3:(10-30)SiO2:(150-450)H2Mixing a silicon source, an aluminum source, polyacrylamide and water according to the molar ratio of O to prepare a guiding agent;
2) preparation of reaction mixture gel: according to (1-4) Na2O:Al2O3:(7-10)SiO2:(100-300)H2Mixing a guiding agent, a silicon source, an alkali source, an aluminum source and water according to the molar ratio of O to prepare reaction mixture gel; wherein, the amount of the guiding agent accounts for 5 to 15 percent based on the total mass of the reaction mixture gel as 100 percent;
3) crystallization of reaction mixture gel: and 2) carrying out crystallization reaction on the reaction mixture gel prepared in the step 2) to prepare the NaY zeolite.
2. The production method according to claim 1,
the silicon source comprises at least one of water glass, silica sol, white carbon black and sodium silicate;
the aluminum source comprises at least one of sodium metaaluminate, high-alkali sodium metaaluminate, aluminum sulfate and aluminum nitrate;
the alkali source comprises at least one of sodium metaaluminate, high-alkali sodium metaaluminate, sodium hydroxide and potassium hydroxide.
3. The preparation method of claim 1, wherein the directing agent is prepared by mixing the silicon source, the aluminum source, the polyacrylamide and the water in the step 1) and then aging the mixture at 10 to 50 ℃ for 4 to 60 hours.
4. The method of claim 1, wherein the preparation of the reaction mixture gel is performed at 30-70 ℃.
5. The method of claim 1, wherein the step 2) of mixing the directing agent, the silicon source, the alkali source, the aluminum source, and the water comprises: firstly, mixing a guiding agent and a silicon source, and then adding an alkali source, an aluminum source and water to prepare reaction mixture gel;
preferably, the alkali source is added first and then the aluminum source.
6. The preparation method according to claim 1, wherein the temperature of the crystallization reaction in the step 3) is 70-100 ℃, and the time of the crystallization reaction is 6-50 h.
7. The preparation method of claim 1, wherein the flaky small-grained NaY zeolite is obtained by filtering, washing and drying after the crystallization reaction in the step 3).
8. A NaY zeolite obtained by the method for producing a NaY zeolite as claimed in any one of claims 1 to 7, which has a crystallinity of 90% or more and a silica-alumina molar ratio of SiO2/Al2O34.5-5.9, grain size of 300nm or less, and sodiumThe nanometer flake NaY zeolite has nanometer flake thickness of 50-100 nm.
9. The NaY zeolite of claim 8, wherein,
the specific surface area of the NaY zeolite is 700m2More than g, and the mesoporous volume is 0.101-0.150cm3Per g, pore volume 0.440cm3More than g;
the crystal grain size of the NaY zeolite is 75-300 nm.
10. The NaY zeolite of claim 8, wherein the amount of the nano-platelet NaY zeolite is 10-60% based on 100% of the number of crystal grains of the NaY zeolite.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114604876A (en) * 2022-03-10 2022-06-10 中国石油大学(北京) Ultrastable Y-type zeolite and its preparing process and application
CN114933314A (en) * 2022-05-16 2022-08-23 河南师范大学 Nano NaY zeolite and preparation method and application thereof

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4215015A (en) * 1979-02-02 1980-07-29 Uop Inc. High octane FCC catalyst
US4299733A (en) * 1980-05-08 1981-11-10 Uop Inc. High octane FCC catalyst
JPH0648725A (en) * 1992-07-30 1994-02-22 Mitsubishi Kasei Corp Production of beta-type zeolite
US20080253959A1 (en) * 2007-03-30 2008-10-16 Johnson Ivy D Synthesis crystalline molecular sieves
US20120093715A1 (en) * 2010-10-19 2012-04-19 Uop Llc Monolithic zeolite structures with and without hierarchical pore structures and methods for producing the same
CN102689910A (en) * 2011-03-23 2012-09-26 中国石油天然气股份有限公司 Synthetic method of mesoporous-microporous Y-type molecular sieve
CN104118885A (en) * 2013-04-23 2014-10-29 中国石油天然气股份有限公司 Synthetic method for NaY zeolite with high silica-alumina ratio
CN104649294A (en) * 2013-11-22 2015-05-27 中国石油天然气集团公司 Method for improving relative crystallinity of synthetic NaY zeolite
CN105293518A (en) * 2014-07-07 2016-02-03 北京化工大学 Method for synthesis of mesoporous molecular sieve from industrial raw materials at low cost
CN106927479A (en) * 2015-12-30 2017-07-07 中国石油化工股份有限公司 A kind of method for preparing mesoporous Y type molecular sieve
US20170274350A1 (en) * 2014-09-12 2017-09-28 Arkema France Zeolite nanocrystal aggregates
CN110156046A (en) * 2019-06-25 2019-08-23 华东理工大学 The preparation method of SSZ-13 molecular sieve and the application of SSZ-13 molecular sieve

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4215015A (en) * 1979-02-02 1980-07-29 Uop Inc. High octane FCC catalyst
US4299733A (en) * 1980-05-08 1981-11-10 Uop Inc. High octane FCC catalyst
JPH0648725A (en) * 1992-07-30 1994-02-22 Mitsubishi Kasei Corp Production of beta-type zeolite
US20080253959A1 (en) * 2007-03-30 2008-10-16 Johnson Ivy D Synthesis crystalline molecular sieves
US20120093715A1 (en) * 2010-10-19 2012-04-19 Uop Llc Monolithic zeolite structures with and without hierarchical pore structures and methods for producing the same
CN102689910A (en) * 2011-03-23 2012-09-26 中国石油天然气股份有限公司 Synthetic method of mesoporous-microporous Y-type molecular sieve
CN104118885A (en) * 2013-04-23 2014-10-29 中国石油天然气股份有限公司 Synthetic method for NaY zeolite with high silica-alumina ratio
CN104649294A (en) * 2013-11-22 2015-05-27 中国石油天然气集团公司 Method for improving relative crystallinity of synthetic NaY zeolite
CN105293518A (en) * 2014-07-07 2016-02-03 北京化工大学 Method for synthesis of mesoporous molecular sieve from industrial raw materials at low cost
US20170274350A1 (en) * 2014-09-12 2017-09-28 Arkema France Zeolite nanocrystal aggregates
CN106927479A (en) * 2015-12-30 2017-07-07 中国石油化工股份有限公司 A kind of method for preparing mesoporous Y type molecular sieve
CN110156046A (en) * 2019-06-25 2019-08-23 华东理工大学 The preparation method of SSZ-13 molecular sieve and the application of SSZ-13 molecular sieve

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
BAYBAS, DEMET ET AL: "Polyacrylamide-clinoptilolite/Y-zeolite composites: Characterization and adsorptive features for terbium", 《JOURNAL OF HAZARDOUS MATERIALS 》 *
KOOHSARYAN, ESMAT ET AL: "Facile and rapid synthesis of highly crystalline mesoporous zeolite FAU", 《MATERIALS LETTERS》 *
LI, DAN ET AL: "Zeolite crystallization in crosslinked chitosan hydrogels: Crystal size control and chitosan removal", 《MICROPOROUS AND MESOPOROUS MATERIALS》 *
LIU, RUIYUN ET AL: "Morphology adjustment of ZSM-5 nanocrystal agglomerates and achievement of improved activity in LDPE catalytic cracking reaction", 《MICROPOROUS AND MESOPOROUS MATERIALS》 *
李倪萍: "多级孔纳米ZSM-5分子筛的制备及催化应用", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 *
狄春雨 等: "阳离子聚丙烯酰胺絮凝回收利用SAPO-34分子筛母液", 《太原理工大学学报》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114604876A (en) * 2022-03-10 2022-06-10 中国石油大学(北京) Ultrastable Y-type zeolite and its preparing process and application
CN114933314A (en) * 2022-05-16 2022-08-23 河南师范大学 Nano NaY zeolite and preparation method and application thereof
CN114933314B (en) * 2022-05-16 2024-03-22 河南师范大学 Nano NaY zeolite and preparation method and application thereof

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