CN113479915A - Preparation method of crystal face oriented growth magnesium hydroxide - Google Patents
Preparation method of crystal face oriented growth magnesium hydroxide Download PDFInfo
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- CN113479915A CN113479915A CN202110787055.1A CN202110787055A CN113479915A CN 113479915 A CN113479915 A CN 113479915A CN 202110787055 A CN202110787055 A CN 202110787055A CN 113479915 A CN113479915 A CN 113479915A
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- 239000013078 crystal Substances 0.000 title claims abstract description 42
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 title claims abstract description 40
- 239000000347 magnesium hydroxide Substances 0.000 title claims abstract description 40
- 229910001862 magnesium hydroxide Inorganic materials 0.000 title claims abstract description 40
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
- 239000012266 salt solution Substances 0.000 claims abstract description 18
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 16
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 16
- 238000002425 crystallisation Methods 0.000 claims abstract description 16
- 230000008025 crystallization Effects 0.000 claims abstract description 16
- 239000000243 solution Substances 0.000 claims abstract description 15
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 14
- 239000008367 deionised water Substances 0.000 claims abstract description 13
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000002002 slurry Substances 0.000 claims abstract description 9
- 238000001035 drying Methods 0.000 claims abstract description 7
- 238000001914 filtration Methods 0.000 claims abstract description 7
- 238000005406 washing Methods 0.000 claims abstract description 7
- 159000000003 magnesium salts Chemical class 0.000 claims abstract description 5
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 239000002244 precipitate Substances 0.000 claims abstract description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 9
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 claims description 8
- 229910001425 magnesium ion Inorganic materials 0.000 claims description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 6
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims description 6
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 4
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims description 4
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 4
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 claims description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 3
- 239000002202 Polyethylene glycol Substances 0.000 claims description 3
- 229920001223 polyethylene glycol Polymers 0.000 claims description 3
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 2
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims description 2
- 235000019341 magnesium sulphate Nutrition 0.000 claims description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims 1
- 238000009826 distribution Methods 0.000 abstract description 10
- 238000010899 nucleation Methods 0.000 abstract description 5
- 230000006911 nucleation Effects 0.000 abstract description 5
- 239000003513 alkali Substances 0.000 abstract description 2
- 238000002955 isolation Methods 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 abstract description 2
- 230000001360 synchronised effect Effects 0.000 abstract description 2
- 239000000047 product Substances 0.000 description 11
- 239000002245 particle Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 229940050906 magnesium chloride hexahydrate Drugs 0.000 description 4
- DHRRIBDTHFBPNG-UHFFFAOYSA-L magnesium dichloride hexahydrate Chemical compound O.O.O.O.O.O.[Mg+2].[Cl-].[Cl-] DHRRIBDTHFBPNG-UHFFFAOYSA-L 0.000 description 4
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 3
- 239000003063 flame retardant Substances 0.000 description 3
- 239000012796 inorganic flame retardant Substances 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- 238000005411 Van der Waals force Methods 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 150000002500 ions Chemical group 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229960002337 magnesium chloride Drugs 0.000 description 1
- 239000008204 material by function Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000002572 peristaltic effect Effects 0.000 description 1
- 229920000307 polymer substrate Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000012716 precipitator Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F5/00—Compounds of magnesium
- C01F5/14—Magnesium hydroxide
- C01F5/20—Magnesium hydroxide by precipitation from solutions of magnesium salts with ammonia
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
The invention discloses a preparation method of crystal face oriented growth magnesium hydroxide. Firstly, adding soluble magnesium salt and an oriented growth agent into deionized water to prepare a salt solution; and then simultaneously adding the salt solution and the ammonia water solution into a nuclear reactor, transferring the formed precipitate slurry into a crystallization kettle for heating crystallization, and finally washing, filtering and drying to obtain the micron-sized hexagonal flaky magnesium hydroxide with crystal face oriented growth and high length-thickness ratio. Based on the crystal growth principle and the nucleation crystallization isolation method, the salt solution and the alkali solution form a two-dimensional liquid film under high-speed rotation, a crystal nucleus with (001) crystal face oriented growth is formed under the action of an oriented growth agent, and then synchronous oriented growth is carried out under a uniform and stable environment. The crystal face of the magnesium hydroxide prepared by the method grows in an oriented mode, the grain size in the a-axis direction and the b-axis direction is 1-4 mu m, the length-thickness ratio is 10-100 mu m, the surface polarity is small, the grain size distribution is uniform, and the method has extremely high industrial application prospect and value.
Description
Technical Field
The invention belongs to the technical field of preparation of inorganic functional materials, and particularly relates to a preparation method of flaky magnesium hydroxide with crystal face oriented growth.
Background
Magnesium hydroxide is a typical compound of a layered structure, in each unit cell, Mg2+At the nodal position of the hexagonal lattice origin, OH-In three Mg2+The upper and lower sides of the formed triangular plane are distributed in a crossed way, and Mg2+Has a coordination number of 6 and two OH groups on the upper and lower sides-. Thus, Mg (OH)2Corresponding to two OH layers-And a layer of Mg2+The three ions form a unit layer. The (101) crystal plane of magnesium hydroxide reflects an increase in the number of unit layers, and the unit layers are formed by van der waals forces and hydrogen bonds, and are crystal planes having polarity. And the (001) plane is a transverse extension of the unit layers, and the inside of each unit layer is bonded by ionic bonds, and is a non-polar plane.
Magnesium hydroxide is used as an environment-friendly material with unique physical and chemical properties, and is widely applied to the fields of wastewater, waste gas and acidic water pollutant treatment, antibiosis, new-generation inorganic flame retardants and the like. As a new generation of inorganic flame retardant material, compared with other inorganic flame retardants, magnesium hydroxide is safe and nontoxic, has stable performance, low production cost and better filling performance, can neutralize acidic and corrosive gases generated by polymer combustion, has good flame retardant effect, simultaneously has smoke abatement effect, excellent performance and wide development prospect.
Different crystal faces of magnesium hydroxide have different polarities and have great influence on the performance of the magnesium hydroxide. If the organic silicon/aluminum composite material is added into an organic polymer as an auxiliary agent such as a flame retardant, the material is easy to agglomerate due to the large surface polarity and poor surface compatibility with the polymer, so that the mechanical property of the material is reduced. Therefore, the surface polarity of the magnesium hydroxide can be controlled by regulating the oriented growth of the crystal face of the magnesium hydroxide, so that the non-polar (001) crystal face of the magnesium hydroxide can be oriented to grow, the growth of the polar (101) crystal face is inhibited, the length-diameter ratio is increased, the compatibility of the magnesium hydroxide and a polymer substrate can be improved, and the performances of flame retardance, smoke suppression and the like of the magnesium hydroxide are further improved.
Disclosure of Invention
The invention provides a preparation method of crystal face oriented growth magnesium hydroxide, which aims to improve the compatibility of the magnesium hydroxide and an organic polymer and strengthen the flame retardant and smoke suppression performance of a material. The crystal face of the magnesium hydroxide prepared by the method grows in an oriented mode, the grain size in the a-axis direction and the b-axis direction is 1-4 mu m, the length-thickness ratio is 10-100 mu m, the surface polarity is small, the grain size distribution is uniform, and the method has extremely high industrial application prospect and value.
The preparation method of crystal face oriented growth magnesium hydroxide comprises the following steps: adding soluble magnesium salt and an oriented growth agent into deionized water to prepare a salt solution; and simultaneously adding the salt solution and the ammonia water solution into a nuclear reactor, transferring the formed precipitate slurry into a crystallization kettle for heating crystallization, and finally washing, filtering and drying to obtain the micron-sized hexagonal flaky magnesium hydroxide with crystal face oriented growth and high length-thickness ratio.
The soluble magnesium salt is selected from one or more of magnesium chloride, magnesium nitrate and magnesium sulfate.
The concentration of magnesium ions in the salt solution is 0.01-6mol/L, and the concentration of the magnesium ions and NH in the ammonia water solution3·H2The molar ratio of O is 1: 1-6.
The orientation growth agent is selected from one or more of ethanol, ethylene glycol, propanol, propylene glycol, glycerol, butanol and polyethylene glycol.
The volume ratio of the oriented growth agent to the deionized water in the salt solution is 1: 0.2-4.
The flow rate of the salt solution and the ammonia solution added into the nuclear reactor is 0.1-500mL/min, and the rotating speed of the nuclear reactor is 1000-8000 rpm.
The temperature for heating crystallization is 40-300 ℃, and the crystallization time is 0.5-24 hours.
The beneficial results are that: based on a crystal growth principle and a nucleation crystallization isolation method, the invention utilizes a two-dimensional limited-area ultrathin nucleation reaction space between a stator and a conical rotor of a nucleation reactor to enable a salt solution and an alkali solution to form a two-dimensional liquid film under high-speed rotation, forcefully promotes the formation of crystal nuclei with (001) crystal face oriented growth and uniform particle size distribution under the action of an oriented growth agent, and then the crystal nuclei are crystallized under the same system environment to ensure synchronous oriented growth of the magnesium hydroxide crystal nuclei under a uniform and stable environment, so as to obtain the micron-sized hexagonal flaky magnesium hydroxide with high length-thickness ratio. The method takes ammonia water as a precipitator, so that the pH value of the nucleating slurry is in a medium alkaline range, the dynamic reaction balance damage caused by the magnesium hydroxide crystal nucleus in a high alkaline environment is avoided, the lattice disorder caused by the aggravation of the surface precipitation reaction is reduced, and the stability of the growth process of the magnesium hydroxide crystal nucleus is ensured. Meanwhile, under the action of an oriented growth agent, the oriented growth of the magnesium hydroxide laminate along the directions of the a axis and the b axis is effectively promoted, and a magnesium hydroxide product with micron-sized particle size, regular sheet-shaped appearance and high length-thickness ratio is obtained. The method has the advantages of convenient operation, simple process flow, low production cost, pure product, high crystallinity, regular appearance and large length-thickness ratio, and meanwhile, the method can be used for continuous production and is very suitable for large-scale production.
Drawings
FIG. 1 is an XRD spectrum of crystal plane-oriented magnesium hydroxide prepared in example 1;
FIG. 2 is an SEM photograph of a crystal-plane-oriented magnesium hydroxide prepared in example 1;
FIG. 3 is a laser particle size distribution diagram of crystal-plane-oriented magnesium hydroxide obtained in example 3.
Detailed Description
Example 1:
weighing 30.50g of magnesium chloride hexahydrate and 2.5mL of absolute ethyl alcohol serving as oriented growth agents, and adding deionized water to prepare 75mL of salt solution; 30.65g of ammonia water with the mass concentration of 25% is added into deionized water to be diluted to obtain 75mL of ammonia water solution. The two solutions enter a nuclear reactor simultaneously at the same flow of 100mL/min through a peristaltic pump, the rotating speed of the nuclear reactor is 3000 r/min, and formed precipitation slurry flows out of the reactor from a discharge hole at the bottom of the nuclear reactor. And crystallizing the slurry obtained by the reaction in a crystallization kettle at 120 ℃ for 6 hours, and filtering, washing and drying to obtain the micron-sized magnesium hydroxide. Ratio I of diffraction peak intensities of (001) crystal face and (101) crystal face of product001/I1011.527, the nonpolar (001) crystal plane preferentially grows, and the particle size distribution D501.391 μm, D902.747 μm.
The product is characterized by the crystal structure by adopting an XRD-6000X-ray powder diffractometer of Shimadzu corporation in Japan, an XRD pattern is shown as figure 1, the comparison with a standard spectrogram of magnesium hydroxide proves that the product is magnesium hydroxide, and the ratio I of the diffraction peak intensities of the crystal face (001) and the crystal face (101) of the product001/I101Growth of a nonpolar (001) crystal plane was promoted as 1.527. The crystal grain size and morphology were observed by scanning electron microscope of model supra55 from ZEISS, Germany. FIG. 2 is an SEM photograph, and it can be seen from the figure that the prepared magnesium hydroxide product is in a hexagonal plate structure, the particle size is between 0.81 and 2.1 μm, and the distribution is uniform.
Example 2:
121.98g of magnesium chloride hexahydrate and 60mL of absolute ethyl alcohol are weighed as oriented growth agents and added into deionized water to prepare 300mL of salt solution; 81.74g of ammonia water with a mass concentration of 25% was added to deionized water to dilute the solution to obtain 300mL of ammonia water solution. The two solutions were passed through a nuclear reactor at the same flow rate and reactor rotation speed as in example 1. And adding the slurry obtained by nucleation into a crystallization kettle, crystallizing for 6 hours at 160 ℃, and filtering, washing and drying to obtain the micron-sized hexagonal flaky magnesium hydroxide. The product has the ratio I of the diffraction peak intensities of the (001) crystal face and the (101) crystal face001/I1011.608, the nonpolar (001) crystal plane preferentially grows, and the particle size distribution D501.134 μm, D90It was 2.123. mu.m.
Example 3:
weighing 20.33g of magnesium chloride hexahydrate and 10mL of oriented growth agent glycerol, and adding deionized water to prepare 50mL of salt solution; 27.25g of ammonia water with a mass concentration of 25% was diluted with deionized water to obtain 50mL of an ammonia water solution. The flow rate of the two solutions through the nuclear reactor and the rotational speed of the reactor were the same as in example 1. Crystallizing the obtained slurry in a crystallization kettle at 80 ℃ for 6 hours, filtering, washing and drying to obtain the micron-sized hexagonal flaky magnesium hydroxide.
The product particle size distribution is tested by adopting a British Malvern 2000 laser particle size analyzer, the nonpolar (001) crystal face of the product preferentially grows, and the particle size distribution D503.726 μm, D906.902 μm.
Example 4:
weighing 20.33g of magnesium chloride hexahydrate and 10mL of polyethylene glycol serving as oriented growth agents, and adding deionized water to prepare 50mL of salt solution; 27.25g of ammonia water with a mass concentration of 25% was diluted with deionized water to obtain 50mL of an ammonia water solution. The flow rate of the two solutions through the nuclear reactor and the rotational speed of the reactor were the same as in example 1. Crystallizing the obtained slurry in a crystallization kettle at 200 deg.C for 6 hr, filtering, washing, and drying to obtainMicron-sized hexagonal flaky magnesium hydroxide. The nonpolar (001) crystal face of the product preferentially grows, I001/I1011.220, particle size distribution D501.840 μm, D90It was 3.178. mu.m.
The present invention has been described in detail, and it should be understood that the detailed description and specific examples, while indicating the preferred embodiment of the invention, are intended for purposes of illustration only and are not intended to limit the scope of the invention.
Claims (7)
1. A preparation method of crystal face oriented growth magnesium hydroxide is characterized by comprising the following specific operations: adding soluble magnesium salt and an oriented growth agent into deionized water to prepare a salt solution; and simultaneously adding the salt solution and the ammonia water solution into a nuclear reactor, transferring the formed precipitate slurry into a crystallization kettle for heating crystallization, and finally washing, filtering and drying to obtain the micron-sized hexagonal flaky magnesium hydroxide with crystal face oriented growth and high length-thickness ratio.
2. The preparation method according to claim 1, wherein the soluble magnesium salt is selected from one or more of magnesium chloride, magnesium nitrate and magnesium sulfate.
3. The method according to claim 1, wherein the concentration of magnesium ions in the salt solution is 0.01 to 6mol/L, and the concentration of magnesium ions and NH in the aqueous ammonia solution3·H2The molar ratio of O is 1: 1-6.
4. The method according to claim 1, wherein the orientation growth agent is one or more selected from ethanol, ethylene glycol, propanol, propylene glycol, glycerol, butanol, and polyethylene glycol.
5. The preparation method of claim 1, wherein the volume ratio of the orientation growth agent to the deionized water in the salt solution is 1: 0.2-4.
6. The method as claimed in claim 1, wherein the flow rate of the salt solution and the ammonia solution into the nuclear reactor is 0.1-500mL/min, and the rotation speed of the nuclear reactor is 1000-8000 rpm.
7. The method according to claim 1, wherein the temperature for thermal crystallization is 40-300 ℃ and the crystallization time is 0.5-24 hours.
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