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CN111924856B - ZSM-57 molecular sieve and preparation method thereof - Google Patents

ZSM-57 molecular sieve and preparation method thereof Download PDF

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CN111924856B
CN111924856B CN201910393482.4A CN201910393482A CN111924856B CN 111924856 B CN111924856 B CN 111924856B CN 201910393482 A CN201910393482 A CN 201910393482A CN 111924856 B CN111924856 B CN 111924856B
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郭鹏
王磊
田鹏
刘中民
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Abstract

本申请公开了一种ZSM‑57分子筛,所述ZSM‑57分子筛为纳米晶粒堆叠的规则的片状。所述ZSM‑57分子筛不仅具有规整的孔道排列且有较短的扩散程,极高的结晶度和较为充裕的接触面积提高了此类沸石的利用效率。The present application discloses a ZSM-57 molecular sieve, the ZSM-57 molecular sieve is in the form of a regular sheet with stacked nano-crystal grains. The ZSM-57 molecular sieve not only has regular channel arrangement and short diffusion path, but also has extremely high crystallinity and relatively abundant contact area, which improves the utilization efficiency of this type of zeolite.

Description

ZSM-57 molecular sieve and preparation method thereof
Technical Field
The invention belongs to the technical field of inorganic materials, and particularly relates to a preparation method of a ZSM-57 molecular sieve single crystal sheet.
Background
ZSM-57 zeolite is a microporous crystalline zeolite having a two-dimensional ten-membered ring and eight-membered ring channel structure. Meanwhile, the ZSM-57 zeolite also has higher thermal stability, hydrothermal stability and adjustable acidity. Therefore, ZSM-57 zeolites have shown high utility in small molecule shape selective catalysis, aromatic alkylation, toluene disproportionation, and long paraffin isomerization.
The ZSM-57 zeolite reported at present has irregular appearance and nonuniform grain size, so that the ten-membered ring channel structure is in disordered stacking arrangement and often has higher mass transfer resistance. The preparation of regular shape and uniform nano zeolite crystal grain is one of the effective approaches to solve the above problems. Compared with conventional disordered ZSM-57 zeolite crystal grains, the ZSM-57 zeolite with regular pore channel arrangement and single crystal disc sheet shape has the advantages of wider mass transfer orientation, high activity, high mechanical strength and the like, so the application of the ZSM-57 zeolite in the chemical industry is increasingly wide.
Usually, more additives, such as amino acids or polyhydroxy high molecular polymers, are required to be introduced to adjust the structure and morphology of the zeolite, which increases the cost and pollutes the environment.
Disclosure of Invention
According to one aspect of the present application, there is provided a ZSM-57 molecular sieve characterized in that,
the ZSM-57 molecular sieve is a regular sheet with stacked nano crystal grains.
Optionally, the ZSM-57 molecular sieve morphology is a pentagonal star-like regular single crystal disc.
Optionally, the particle size of the zsm-57 molecular sieve is 0.2-1 μm.
Optionally, the length-diameter ratio of the ZSM-57 molecular sieve is 1-100; the thickness of the ZSM-57 molecular sieve is 20-300 nm.
Alternatively, the ZSM-57 molecular sieve pore channels are oriented.
Optionally, the ZSM-57 molecular sieve has a silicon-aluminum atomic ratio of 15-40.
Optionally, the XRD pattern of the ZSM-57 molecular sieve contains diffraction peaks at the following positions:
Figure BDA0002057373680000021
Figure BDA0002057373680000022
Figure BDA0002057373680000023
Figure BDA0002057373680000024
Figure BDA0002057373680000025
Figure BDA0002057373680000026
Figure BDA0002057373680000027
Figure BDA0002057373680000028
Figure BDA0002057373680000029
Figure BDA00020573736800000210
optionally, the specific surface area of the ZSM-57 molecular sieve is 400-500 m2/g;
The specific surface area of the micropores of the ZSM-57 molecular sieve is 300-400 m2/g;
The micropore volume of the ZSM-57 molecular sieve is 0.1-0.5 m3/g。
According to one aspect of the application, a preparation method of a directional pore channel arranged ZSM-57 molecular sieve sheet single crystal with low pollution and high efficiency is provided. The preparation method is simple, high in efficiency, convenient to operate, low in pollution and suitable for industrial production.
The method for preparing the ZSM-57 molecular sieve is characterized by comprising the following steps of:
(1) the method comprises the steps of providing a source containing T element, a source containing A element and an alkali source OH-Mixing the raw materials of the organic template agent R and water to obtain an initial mixture;
(2) carrying out hydrothermal crystallization on the initial mixture obtained in the step (1) to obtain the ZSM-57 molecular sieve;
wherein the T element source is selected from at least one of group IV A elements;
the A element source is selected from at least one of group IIIA elements;
the alkali source OH-Is a source of an alkali metal and/or a source of an alkaline earth metal;
the organic template R is selected from at least one of compounds with a chemical structural formula shown in formula I:
Figure BDA0002057373680000031
in the formula I, n is 3-10; r1,R2,R3,R4,R5,R6Independently selected from C1~C6At least one of the hydrocarbon groups of (a); x1 -、X2 -Independently selected from OH-And a halogen element anion.
Alternatively, R1,R2,R3,R4,R5,R6Independently selected from C1~C6At least one of alkyl groups of (a).
Alternatively, R1,R2,R3,R4,R5,R6Independently selected from C1~C6At least one of linear alkyl groups of (a).
Alternatively, R1,R2,R3,R4,R5,R6Independently selected from C1~C6At least one of the alkyl groups having a branch.
Alternatively, R1,R2,R3,R4,R5,R6Independently selected from C1~C5At least one of alkyl groups of (a).
Alternatively, R1,R2,R3,R4,R5,R6Independently selected from C1~C5At least one of linear alkyl groups of (a).
Alternatively, R1,R2,R3,R4,R5,R6Independently selected from C1~C5At least one of the alkyl groups having a branch.
Optionally, the lower limit of the hydrothermal crystallization temperature is selected from 140 ℃, 145 ℃, 150 ℃, 155 ℃. 160 ℃, 165 ℃, 170 ℃, 175 ℃, 180 ℃, 185 ℃, 190 ℃ or 195 ℃; the upper limit is selected from 145 deg.C, 150 deg.C, 155 deg.C. 160 ℃, 165 ℃, 170 ℃, 175 ℃, 180 ℃, 185 ℃, 190 ℃, 195 ℃ or 200 ℃.
Optionally, the lower limit of the hydrothermal crystallization time is selected from 24 hours, 48 hours, 72 hours, 96 hours, 120 hours, 144 hours, 168 hours, 192 hours, 216 hours, 240 hours, 264 hours, 288 hours, 312 hours, 336 hours, 360 hours, 384 hours, 408 hours, 432 hours, or 456 hours; the upper limit is selected from 48 hours, 72 hours, 96 hours, 120 hours, 144 hours, 168 hours, 192 hours, 216 hours, 240 hours, 264 hours, 288 hours, 312 hours, 336 hours, 360 hours, 384 hours, 408 hours, 432 hours, 456 hours, or 480 hours.
Specifically, the method comprises the following steps:
(1) TO is a tetravalent oxide2Of a trivalent oxide A2O3OH as a source of alkali-Mixing an organic template agent R and water to obtain an initial mixture;
(2) placing the mixture obtained in the step (1) at 140-200 ℃ for hydrothermal crystallization for 24-480 hours to obtain the ZSM-57 molecular sieve with the directional pore channel arrangement;
wherein TO in the initial mixture2、A2O3OH as a source of alkali-R and H2The molar ratio of O is: TO2/Y2O3Is in the range of 10 to 999,
OH-/TO2is in the range of 0.01 to 1.0,
H2O/TO2is in the range of 10 to 120,
R/TO20.05 to 1.0;
r is selected from at least one of the compounds with the chemical structural formula shown in the formula I:
Figure BDA0002057373680000041
wherein n is 3-10.
Optionally, a source of T element, a source of A element, a source of an alkali OH in the initial mixture-Organic templating agents R and H2The molar ratio of O is:
TO2/A2O3is in the range of 10 to 999,
OH-/TO2is in the range of 0.01 to 1.0,
H2O/TO2is in the range of 10 to 120,
R/TO20.05 to 1.0;
wherein, T element is sourced from TO2Based on the mole number of the element A, the source of the element A is A2O3Based on the mole number of the alkali source OH-With OH contained therein-In moles of the organic template R, H in moles of the organic template R itself2O is in moles on its own.
Optionally, R/TO in the initial mixture2The lower limit of the molar ratio range of (a) is selected from 0.06: 1. 0.07: 1. 0.08: 1. 0.09: 1. 0.1: 1 or 0.12: 1, upper limit selected from 0.15: 1. 0.2: 1. 0.3: 1. 0.4: 1. 0.5: 1. 0.6: 1. 0.7: 1. 0.8: 1. 0.9: 1 or 1.0: 1.
optionally, R/TO in the initial mixture2The molar ratio of (A) to (B) is: 0.08-0.8: 1.
optionally, OH in the initial mixture-/TO2The lower limit of the molar ratio range of (a) is selected from 0.01: 1. 0.02: 0.03, 0.04: 1. 0.045: 1 or 0.05: 1, upper limit selected from 0.5: 1. 0.6: 1. 0.65: 1. 0.7: 1 or 0.8: 1.
optionally, TO in the initial mixture2/A2O3The lower limit of the molar ratio range of (a) is selected from 10, 20, 25, 30, 40, 50, 60, 70, 80, 90, 100, 120, 150, 180, 200, 250, 300, 400, 500, 600, 700, 800 or 900; the upper limit is selected from 20, 25, 30, 40, 50, 60, 70, 80, 90, 100, 120, 150, 180, 200, 250, 300, 400, 500, 600, 700, 800, 900, or 999.
Alternatively, H in the initial mixture2O/TO2The lower limit of the molar ratio range of (a) is selected from 10, 20, 30, 40, 50, 60, 70, 80, 90, 100 or 110; the upper limit is selected from 20, 30, 40, 50, 60, 70, 80, 90, 100, 110, or 120.
Optionally, the T element source is selected from at least one of a silicon source, a germanium source and a tin source;
the A element source is at least one selected from aluminum source, boron source and gallium source;
the alkali source OH-At least one selected from alkali metal hydroxides and alkaline earth metal hydroxides.
Optionally, the silicon source is selected from at least one of tetraethoxysilane, silica gel, silicic acid, white carbon black, silica sol, water glass and diatomite;
the germanium source is germanium oxide;
the tin source is at least one of tin oxide and tin chloride;
the aluminum source is selected from at least one of aluminum isopropoxide, sodium aluminate, aluminum foil, aluminum sulfate, aluminum chloride, aluminum nitrate, aluminum hydroxide and pseudo-boehmite;
the boron source is at least one of boric acid, sodium borate and boron oxide;
the gallium source is selected from at least one of gallium nitrate and gallium trichloride;
the alkali source OH-At least one selected from sodium hydroxide, potassium hydroxide and cesium hydroxide.
Alternatively, in formula I, n ═ 3-7; r1,R2,R3,R4,R5,R6Independently selected from C1~C3At least one of alkyl groups of (a).
Optionally, the organic template agent R is 1, 5-hexaethyl pentanediammonium bromide.
Optionally, step (1) comprises: to A element source and alkali source OH-And adding a T element source into the mixture of the organic template agent R and the water, and mixing to obtain an initial mixture.
Optionally, step (1) comprises: to A element source and alkali source OH-And adding a T element source into the mixture of the organic template agent R and the water, and mixing to obtain an initial mixture.
Optionally, step (2) comprises: and (2) carrying out hydrothermal crystallization on the initial mixture obtained in the step (1) at the temperature of 140-200 ℃ for 24-480 hours, and separating, washing and drying the obtained product to obtain the ZSM-57 molecular sieve.
Based on the principle of zeolite preparation, framework four connecting atoms in zeolite can be replaced by other metals (germanium source, tin source, aluminum source and gallium source) or non-metal atoms (silicon source and boron source) and the framework structure of zeolite crystal is kept the same.
All conditions in this application that relate to a numerical range can be independently selected from any point within the numerical range.
In this application "C1~C6"and the like refer to the number of carbon atoms which a group contains.
In the present application, an "alkyl group" is a group formed by losing any one hydrogen atom on the molecule of an alkane compound.
In this application, a "hydrocarbyl group" is a group formed by the loss of one hydrogen atom on a carbon atom in a hydrocarbon molecule. The hydrocarbon is a carbohydrate, for example, the alkane, alkene, alkyne are all hydrocarbons.
The beneficial effects that this application can produce include:
1) according to the method provided by the application, the prepared ZSM-57 has a regular appearance and a directionally distributed zeolite pore channel structure;
2) according to the method provided by the application, the prepared ZSM-57 has extremely high crystallinity and relatively abundant contact area, so that the sieving utilization efficiency of the zeolite is improved;
3) the ZSM-57 prepared by the method has extremely high length-diameter ratio and shorter diffusion path, thereby improving the film forming efficiency of the zeolite sheets.
Drawings
Figure 1 is an XRD spectrum of the sample of example 1.
FIG. 2 is a SEM photograph of a sample of example 1.
FIG. 3 is a transmission electron micrograph of a selected area of the sample of example 1.
FIG. 4 is a scanning electron micrograph of a sample of comparative example 1.
Detailed Description
The invention is illustrated by the following examples, which are not intended to limit the scope of the invention. The starting materials, templating agents and solvents in the examples of the present invention were all purchased commercially, unless otherwise specified.
The molar ratio of Si to Al in the product is Si/Al atomic ratio in the examples.
The analysis method in the examples of the present invention is as follows:
x-ray powder diffraction phase analysis (XRD) was performed using X' Pert PRO X-ray diffractometer [ Cu target, ka radiation source (λ ═ 0.15418nm), voltage 40kV, current 40mA ], of pananace (PANalytical), netherlands.
SEM topography analysis was performed using a Hitachi (SU8020) scanning electron microscope.
Selective electron diffraction analysis was performed using a JEOL (2100) type transmission electron microscope.
Example 1
The initial gel was formulated in the following molar ratios: SiO 22/Al2O3=100,OH-/SiO2=0.4,R/SiO2=0.2,H2O/SiO2Sodium aluminate, potassium hydroxide and 1, 5-hexaethyl pentanediammonium bromide are respectively dissolved in deionized water, and then white carbon black is added under the condition of continuous stirring. Then the mixture is put into a 100ml crystallization kettle to react for 168 hours at 160 ℃.
And (3) placing the cooled reaction liquid into a water bath, standing for 5 hours to generate obvious layering, wherein beige solid at the lower layer is ZSM-57 zeolite, separating, washing, drying and roasting (the roasting temperature is 550 ℃ and the roasting time is 8 hours) to obtain a sample, wherein the number of the sample is ZSM-57-1, and the yield of the ZSM-57-1 is 91% based on the weight of the added silicon dioxide.
XRD analysis (XRD spectrogram is shown in figure 1) shows that the sample is ZSM-57 zeolite, and the molar ratio of silicon to aluminum is 21; SEM characterization (the SEM image is shown in FIG. 2) confirmed that the sample morphology is pentagonal disk-shaped with nano-small crystal grain stacking, the particle size is 2 μm, and the thickness is about 20 nm.
Examples 2 to 5
The specific compounding ratio and crystallization conditions are shown in table 1, and the specific compounding process is the same as that of example 1.
XRD analysis is carried out on the prepared sample, the data result is similar to that of the sample shown in the table 2, namely, the position and the shape of the peak are the same, and the relative kurtosis of the peak fluctuates within the range of +/-10% according to the change of the preparation conditions, which shows that the prepared product has the characteristics of a ZSM-57 structure.
TABLE 1 ingredient and crystallization conditions for molecular sieve preparation
Figure BDA0002057373680000071
Figure BDA0002057373680000081
Table 2 XRD results for the sample of example 1
Figure BDA0002057373680000082
Comparative example 1
Mixing sodium hydroxide, 1, 5-hexaethyl pentanediammonium bromide, sodium aluminate, water and white carbon black, and preparing according to the following molar ratio: SiO 22/Al2O3=60,OH-/SiO2=0.6,R/SiO2=0.15,H2O/SiO 240. The mixture was then stirred in a 50 ℃ water bath to a homogeneous gel and aged for 12 hours while stirring. And transferring the gel into a hydrothermal crystallization kettle, heating to 160 ℃, carrying out hydrothermal crystallization for 168 hours, then naturally cooling, filtering and drying to obtain zeolite raw powder, and marking the zeolite raw powder as a sample ZSM-57-D1. XRD tests prove that the ZSM-57-D1 sample is ZSM-57 zeolite, small-grain aggregates are observed in a low-power SEM, and a ZSM-57 pentagonal disc with a regular surface is not formed, as shown in figure 4. The yield of ZSM-57 was 86% based on the weight of silica charged. Comparative example description: the aging of the gel affects the morphology of the ZSM-57 molecular sieve, and the obtained ZSM-57 sample does not form a regular single crystal disc and only presents a small particle aggregation state with the same crystal orientation.
Experimental example 6
The sample obtained in example 1 is calcined at 550 ℃ for 8 hours by introducing air to remove the template agent, and then the specific surface area and the pore volume of the sample are tested, wherein the sample has high BET specific surface area of 456m2The specific surface area and the volume of each micropore calculated according to the t-plot method are 316m2G and 0.16cm3/g。
The samples prepared in examples 2 to 5 have similar BET specific surface areas to those tested for the sample of example 1.
Experimental example 7
And (3) introducing air into the sample obtained in the example 1 at 550 ℃ to roast for 8 hours to remove the template agent, and then testing the crystal plane orientation of the sample by adopting a transmission electron microscope. From the selected area electron diffraction pattern (FIG. 3), it can be found that the zeolite sheet orientation of ZSM-57 is [100], i.e. the ten-member ring channel orientation of the zeolite.
The samples prepared in examples 2-5 were similar to the transmission electron mirror image obtained from the sample testing of example 1.
Although the present application has been described with reference to a few embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the application as defined by the appended claims.

Claims (8)

1.一种ZSM-57分子筛,其特征在于,所述ZSM-57分子筛为纳米晶粒堆叠的五角星状规则的片状,所述片状的方向为[100],所述ZSM-57分子筛的长径比为1~100;所述ZSM-57分子筛的厚度为20~300nm。1. a ZSM-57 molecular sieve, it is characterized in that, described ZSM-57 molecular sieve is the regular flake of the five-pointed star shape that nanocrystalline grain stacks, and the direction of described flake is [100], and described ZSM-57 molecular sieve is The aspect ratio of the ZSM-57 molecular sieve is 1-100; the thickness of the ZSM-57 molecular sieve is 20-300 nm. 2.根据权利要求1所述的ZSM-57分子筛,其特征在于,所述ZSM-57分子筛的粒径为0.2~1μm。2 . The ZSM-57 molecular sieve according to claim 1 , wherein the particle size of the ZSM-57 molecular sieve is 0.2-1 μm. 3 . 3.根据权利要求1所述的ZSM-57分子筛,其特征在于,所述ZSM-57分子筛的比表面积为400~500m2/g;3. The ZSM-57 molecular sieve according to claim 1, wherein the ZSM-57 molecular sieve has a specific surface area of 400-500 m 2 /g; 所述ZSM-57分子筛的微孔比表面积为300~400m2/g;The micropore specific surface area of the ZSM-57 molecular sieve is 300-400 m 2 /g; 所述ZSM-57分子筛的微孔容积为0.1~0.5m3/g。The micropore volume of the ZSM-57 molecular sieve is 0.1-0.5 m 3 /g. 4.一种制备权利要求1至3任一项所述的ZSM-57分子筛的方法,其特征在于,包括以下步骤:4. a method for preparing the ZSM-57 molecular sieve described in any one of claims 1 to 3, is characterized in that, comprises the following steps: (1)将含有T元素源、A元素源、碱源OH-、有机模板剂R和水的原料混合,得到初始混合物;(1) mixing raw materials containing T element source, A element source, alkali source OH , organic template R and water to obtain an initial mixture; (2)将步骤(1)中所得到的初始混合物水热晶化,得到所述ZSM-57分子筛;(2) hydrothermal crystallization of the initial mixture obtained in step (1) to obtain the ZSM-57 molecular sieve; 其中,所述步骤(1)和(2)之间不包括凝胶陈化的步骤;Wherein, the step of gel ageing is not included between the steps (1) and (2); 其中,所述T元素源选自IV A族元素中的至少一种;Wherein, the T element source is selected from at least one of IV A group elements; 所述A元素源选自III A族元素中的至少一种;The A element source is selected from at least one of the III A group elements; 所述碱源OH-为碱金属源和/或碱土金属源;The alkali source OH- is an alkali metal source and/or an alkaline earth metal source; 有机模板剂R为1,5-六乙基戊二铵溴代物;The organic template R is 1,5-hexaethylpentanediammonium bromide; 所述初始混合物中的T元素源、A元素源、碱源OH-、有机模板剂R和H2O的摩尔比为:The molar ratio of T element source, A element source, alkali source OH , organic template agent R and H 2 O in the initial mixture is: TO2/A2O3=10~999,TO 2 /A 2 O 3 =10~999, OH-/TO2=0.01~1.0,OH /TO 2 =0.01~1.0, H2O/TO2=10~120,H 2 O/TO 2 =10~120, R/TO2=0.05~1.0;R/TO 2 =0.05~1.0; 其中,T元素源的摩尔数以TO2的摩尔数计,A元素源的摩尔数以A2O3的摩尔数计,碱源OH-的摩尔数以其含有的OH-的摩尔数计,有机模板剂R的摩尔数以其自身的摩尔数计,H2O的摩尔数以其自身的摩尔数计。Among them, the number of moles of T element source is calculated by the number of moles of TO 2 , the number of moles of element A is calculated by the number of moles of A2O3, the number of moles of OH- of the alkali source is calculated by the number of moles of OH- it contains, The number of moles of the organic template R is based on the number of moles of itself, and the number of moles of H 2 O is based on the number of moles of itself. 5.根据权利要求4所述的方法,其特征在于,所述T元素源选自硅源、锗源、锡源中的至少一种;5. The method according to claim 4, wherein the T element source is selected from at least one of a silicon source, a germanium source, and a tin source; 所述A元素源选自铝源、硼源、镓源中的至少一种;The A element source is selected from at least one of an aluminum source, a boron source, and a gallium source; 所述碱源OH-选自碱金属氢氧化物、碱土金属氢氧化物中至少一种。The alkali source OH- is selected from at least one of alkali metal hydroxide and alkaline earth metal hydroxide. 6.根据权利要求5所述的方法,其特征在于,所述硅源选自正硅酸乙酯、硅胶、硅酸、白炭黑、硅溶胶、水玻璃、硅藻土中至少一种;6. The method according to claim 5, wherein the silicon source is selected from at least one of ethyl orthosilicate, silica gel, silicic acid, white carbon black, silica sol, water glass, and diatomaceous earth; 所述锗源为氧化锗;The germanium source is germanium oxide; 所述锡源选自氧化锡、氯化锡中的至少一种;Described tin source is selected from at least one in tin oxide, tin chloride; 所述铝源选自异丙醇铝、铝酸钠、铝箔、硫酸铝、氯化铝、硝酸铝、氢氧化铝、拟薄水铝石中的至少一种;The aluminum source is selected from at least one of aluminum isopropoxide, sodium aluminate, aluminum foil, aluminum sulfate, aluminum chloride, aluminum nitrate, aluminum hydroxide, and pseudo-boehmite; 所述硼源选自硼酸、硼酸钠、氧化硼中的至少一种;The boron source is selected from at least one of boric acid, sodium borate and boron oxide; 所述镓源选自硝酸镓、三氯化镓中的至少一种;The gallium source is selected from at least one of gallium nitrate and gallium trichloride; 所述碱源OH-选自氢氧化钠、氢氧化钾、氢氧化铯中的至少一种。The alkali source OH- is selected from at least one of sodium hydroxide, potassium hydroxide and cesium hydroxide. 7.根据权利要求4所述的方法,其特征在于,步骤(1)包括:向A元素源、碱源OH-、有机模板剂R和水的混合物中加入T元素源,混合,得到初始混合物。7. method according to claim 4, is characterized in that, step (1) comprises: to the mixture of A element source, alkali source OH - , organic template agent R and water, add T element source, mix, obtain initial mixture . 8.根据权利要求4所述的方法,其特征在于,所述水热晶化的条件为:140~200℃下水热晶化24~480小时。8 . The method according to claim 4 , wherein the conditions for the hydrothermal crystallization are: hydrothermal crystallization at 140-200° C. for 24-480 hours. 9 .
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