CN111995882A - Porous calcium silicate rare earth ion-loaded filler powder and preparation method thereof - Google Patents
Porous calcium silicate rare earth ion-loaded filler powder and preparation method thereof Download PDFInfo
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- CN111995882A CN111995882A CN202010770672.6A CN202010770672A CN111995882A CN 111995882 A CN111995882 A CN 111995882A CN 202010770672 A CN202010770672 A CN 202010770672A CN 111995882 A CN111995882 A CN 111995882A
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- calcium silicate
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- 229910052918 calcium silicate Inorganic materials 0.000 title claims abstract description 86
- 239000000378 calcium silicate Substances 0.000 title claims abstract description 86
- 229910052761 rare earth metal Inorganic materials 0.000 title claims abstract description 72
- -1 calcium silicate rare earth ion Chemical class 0.000 title claims abstract description 41
- 239000000843 powder Substances 0.000 title claims abstract description 36
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 239000000945 filler Substances 0.000 title claims description 31
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 claims abstract description 72
- 238000003756 stirring Methods 0.000 claims abstract description 31
- 150000002910 rare earth metals Chemical class 0.000 claims abstract description 30
- 239000000725 suspension Substances 0.000 claims abstract description 24
- 239000002245 particle Substances 0.000 claims abstract description 20
- 238000005470 impregnation Methods 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 238000002156 mixing Methods 0.000 claims abstract description 16
- 239000002270 dispersing agent Substances 0.000 claims abstract description 13
- 238000001035 drying Methods 0.000 claims abstract description 11
- 239000002243 precursor Substances 0.000 claims abstract description 11
- 238000001694 spray drying Methods 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract description 6
- 238000005406 washing Methods 0.000 claims abstract description 6
- 238000000227 grinding Methods 0.000 claims description 14
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 claims description 10
- 229910052746 lanthanum Inorganic materials 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 6
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 6
- 238000001027 hydrothermal synthesis Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 229910052684 Cerium Inorganic materials 0.000 claims description 5
- 150000007942 carboxylates Chemical group 0.000 claims description 5
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 claims description 5
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- RYYKJJJTJZKILX-UHFFFAOYSA-M sodium octadecanoate Chemical compound [Na+].CCCCCCCCCCCCCCCCCC([O-])=O RYYKJJJTJZKILX-UHFFFAOYSA-M 0.000 claims description 4
- WGTYBPLFGIVFAS-UHFFFAOYSA-M tetramethylammonium hydroxide Chemical compound [OH-].C[N+](C)(C)C WGTYBPLFGIVFAS-UHFFFAOYSA-M 0.000 claims description 4
- 150000001875 compounds Chemical group 0.000 claims description 3
- 238000010298 pulverizing process Methods 0.000 claims description 3
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 claims description 3
- 235000019982 sodium hexametaphosphate Nutrition 0.000 claims description 3
- 229940073455 tetraethylammonium hydroxide Drugs 0.000 claims description 3
- LRGJRHZIDJQFCL-UHFFFAOYSA-M tetraethylazanium;hydroxide Chemical compound [OH-].CC[N+](CC)(CC)CC LRGJRHZIDJQFCL-UHFFFAOYSA-M 0.000 claims description 3
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 claims description 3
- 150000001785 cerium compounds Chemical group 0.000 claims description 2
- QQZMWMKOWKGPQY-UHFFFAOYSA-N cerium(3+);trinitrate;hexahydrate Chemical compound O.O.O.O.O.O.[Ce+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O QQZMWMKOWKGPQY-UHFFFAOYSA-N 0.000 claims description 2
- ICAKDTKJOYSXGC-UHFFFAOYSA-K lanthanum(iii) chloride Chemical compound Cl[La](Cl)Cl ICAKDTKJOYSXGC-UHFFFAOYSA-K 0.000 claims description 2
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 claims description 2
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 claims description 2
- HKVFISRIUUGTIB-UHFFFAOYSA-O azanium;cerium;nitrate Chemical compound [NH4+].[Ce].[O-][N+]([O-])=O HKVFISRIUUGTIB-UHFFFAOYSA-O 0.000 claims 1
- HVMFKXBHFRRAAD-UHFFFAOYSA-N lanthanum(3+);trinitrate;hydrate Chemical compound O.[La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O HVMFKXBHFRRAAD-UHFFFAOYSA-N 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 claims 1
- 229920000642 polymer Polymers 0.000 abstract description 9
- 239000012767 functional filler Substances 0.000 abstract 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 abstract description 2
- 239000002131 composite material Substances 0.000 abstract description 2
- 239000003063 flame retardant Substances 0.000 abstract description 2
- 238000012545 processing Methods 0.000 abstract description 2
- MRELNEQAGSRDBK-UHFFFAOYSA-N lanthanum oxide Inorganic materials [O-2].[O-2].[O-2].[La+3].[La+3] MRELNEQAGSRDBK-UHFFFAOYSA-N 0.000 description 7
- 238000011068 loading method Methods 0.000 description 5
- 229910000420 cerium oxide Inorganic materials 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 4
- 239000002861 polymer material Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- FYDKNKUEBJQCCN-UHFFFAOYSA-N lanthanum(3+);trinitrate Chemical compound [La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FYDKNKUEBJQCCN-UHFFFAOYSA-N 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000012763 reinforcing filler Substances 0.000 description 2
- 230000032683 aging Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 230000000051 modifying effect Effects 0.000 description 1
- 238000007709 nanocrystallization Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/28—Compounds of silicon
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/18—Oxygen-containing compounds, e.g. metal carbonyls
- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
- C08K5/098—Metal salts of carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K9/00—Use of pretreated ingredients
- C08K9/12—Adsorbed ingredients, e.g. ingredients on carriers
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- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/006—Combinations of treatments provided for in groups C09C3/04 - C09C3/12
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/04—Physical treatment, e.g. grinding, treatment with ultrasonic vibrations
- C09C3/041—Grinding
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- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/06—Treatment with inorganic compounds
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- 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
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- C08K3/20—Oxides; Hydroxides
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- C08K3/20—Oxides; Hydroxides
- C08K3/22—Oxides; Hydroxides of metals
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Abstract
The invention discloses a functional filler prepared by porous calcium silicate loaded rare earth ions and a preparation method thereof, wherein the porous calcium silicate raw material is added with water and a dispersant according to the weight proportion to prepare a suspension; preparing a soluble precursor of a rare earth component and water into impregnation liquid according to a weight ratio, mixing the porous calcium silicate suspension and the rare earth component impregnation liquid, adjusting the pH value of the system to 8-11, and uniformly stirring; after the reaction is finished, directly spray-drying or drying and roasting after filtering and washing(ii) a Finally, after crushing and scattering, obtaining porous calcium silicate loaded rare earth ion powder with the average particle size of 1-10 mu m and the specific surface area of 150-200 m2(ii) in terms of/g. The invention improves and enhances the processing property, the mechanical property, the flame retardant property and the like of the polymer composite material product; meanwhile, the large specific surface area of the porous calcium silicate can also provide a good carrier environment for various active components.
Description
Technical Field
The invention belongs to the field of inorganic functional fillers, and particularly relates to porous calcium silicate rare earth ion-loaded filler powder and a preparation method thereof.
Background
The enhancement modification of the polymer material is an important component for improving the application performance of the polymer product, which is the key point of research in the fields of polymer material science and engineering, and the design of the reinforcing filler is an effective, universal and cheap means for the enhancement modification of the polymer material. With the enhancement of social environmental awareness, the research on non-petroleum-based green functional reinforcing filler is one of the future development trends in the field of polymer reinforcement.
When the rare earth element filled polymer is acted by external force, transient huge complex compounds can be formed between the rare earth element and polymer molecules, so that the aging resistance, fatigue resistance, heat resistance, oil resistance and other properties of the filled polymer material are obviously improved. The research trend in the field of rare earth reinforced modified polymers is nanocrystallization, multifunction and low cost. However, rare earth particles are easy to agglomerate after being nanocrystallized, so that the reinforcing and modifying effect is greatly reduced, and how to ensure that nanoscale rare earth particles are uniformly dispersed in a polymer system becomes a precondition for realizing the rare earth functionality, a functional filler capable of being prepared by loading rare earth ions and a preparation method thereof are needed.
Disclosure of Invention
The invention aims to provide a filler powder product of porous calcium silicate loaded with rare earth ions, which realizes the uniform dispersion of rare earth components and the surface modification of porous calcium silicate and can be widely applied to the fields of polymers, plastics, catalysis and the like.
The invention also aims to provide a preparation method of the porous calcium silicate rare earth ion-loaded filler powder product, which is low in cost and easy for industrial production.
In order to achieve the purpose of the invention, the invention provides a preparation method of porous calcium silicate rare earth ion-loaded filler powder, which comprises the following steps: adding water and a dispersing agent into a porous calcium silicate raw material according to a weight ratio to prepare a suspension;
1) preparing a soluble precursor of a rare earth component into impregnation liquid in water according to a weight ratio, wherein the rare earth ion component is in a lanthanum or cerium compound form, and the compound form is an oxide or carboxylate form; the proportion of the rare earth component and the active calcium silicate is 1.5 to 30 percent; when the double rare earth ion component is adopted, the ratio of two metal elements, namely lanthanum and cerium, is 2: 1 to 1: 2;
2) mixing the porous calcium silicate suspension with the rare earth component impregnation liquid, adjusting the pH value of the system to 8-11, and uniformly stirring; after the reaction is finished, directly carrying out spray drying or drying and roasting after filtering and washing;
3) finally, after crushing and scattering, obtaining porous calcium silicate loaded rare earth ion powder with the average particle size of 1-10 mu m and the specific surface area of 150-200 m2/g。
Further, the porous calcium silicate is prepared by hydrothermal synthesis, the average particle size of the porous calcium silicate is 1-5 mu m, and the specific surface area of the porous calcium silicate is 170-300 m2/g。
Further, the porous calcium silicate raw material in the step 1) is refined through a grinding and stripping machine; the stirring speed is 400-1500 rpm, the grinding and peeling time is 1-2 hours, and the content of the suspension during grinding and peeling is 15-35%.
Further, the addition amount of the dispersing agent in the step 1) is 0.5-1.5% of the weight of the porous calcium silicate, and the preferable addition proportion is 0.5-1.0% of the porous calcium silicate; the dispersing agent is one of sodium polyacrylate, sodium stearate and sodium hexametaphosphate; the stirring speed is 400-500 rpm, the stirring time is 0.5-1 hour, and the solid content of the suspension is 15-25%.
Further, the rare earth soluble precursor in the step 2) is one or more of hydrated lanthanum nitrate, lanthanum chloride, cerium nitrate hexahydrate or ammonium ceric nitrate; the mass fraction of the impregnation liquid is 1-10%.
Further, the alkaline substance for adjusting the pH value in step 3) is one of ammonia water, tetraethylammonium hydroxide or tetramethylammonium hydroxide, and it is preferably ammonia water.
Further, the mixing and stirring time of the porous calcium silicate suspension and the impregnation liquid in the step 3) is 5-40 minutes, and the mixing and stirring temperature is 30-75 ℃.
Further, the temperature of the spray drying in the step 3) is 350-450 ℃; the drying temperature is 105-120 ℃, the roasting temperature is 350-450 ℃, and the roasting time is 2-4 hours.
Further, the crushing and breaking in the step 4) are carried out in a high-speed crusher, a breaker or a high-speed mechanical impact mill at 1000 rpm-4500 rpm for 1 min-10 min.
The filler powder is subjected to dispersed loading through porous calcium silicate, the average particle size of the filler powder is 1-10 mu m, and the specific surface area of the filler powder is 150-200 m2The mass ratio of the rare earth ion component to the active calcium silicate is 1 to 30 percent.
Drawings
Fig. 1 is a schematic flow chart of a preparation method of porous calcium silicate-loaded rare earth ion filler powder.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention will be described in further detail with reference to the following embodiments and accompanying drawings.
As shown in fig. 1, a method for preparing a functional filler by using porous calcium silicate loaded rare earth ions, which comprises the following steps:
examples 1
1) Preparing a soluble precursor of a rare earth component into impregnation liquid in water according to a weight ratio, wherein the rare earth ion component is in the form of lanthanum or cerium oxide or carboxylate; lanthanum oxide with a rare earth component to active calcium silicate ratio of 30% when a double rare earth ionic component is used, the ratio of the two metal elements lanthanum and cerium is 2: 1;
2) the porous calcium silicate is prepared by hydrothermal synthesis, the average particle size of the porous calcium silicate is 1 μm, and the specific surface area is 170m2(ii) in terms of/g. Refining the porous calcium silicate raw material by a grinding and stripping machine; the stirring speed is 500 r/min, the grinding and peeling time is 1 hour, and the content of the suspension during grinding and peeling is 15 percent.
3) Mixing the porous calcium silicate suspension with the rare earth component impregnation liquid, adjusting the pH value of the system to 9, uniformly stirring, and adjusting the pH value to obtain an alkaline substance which is ammonia water; after the reaction is finished, directly carrying out spray drying or drying and roasting after filtering and washing, wherein the addition amount of the dispersing agent is 0.5 percent of the weight of the porous calcium silicate, the dispersing agent is sodium stearate, the mixing and stirring time of the porous calcium silicate suspension and the impregnation liquid is 5 minutes, the mixing and stirring temperature is 30 ℃, the stirring speed is 400 r/m, the stirring time is 0.5 hour, and the solid content of the suspension is 15 percent. The rare earth soluble precursor is hydrated lanthanum nitrate, and the temperature of spray drying is 360 ℃; the drying temperature is 110 ℃, the roasting temperature is 350 ℃, and the roasting time is 2 hours.
4) Finally, after crushing and scattering, obtaining porous calcium silicate loaded rare earth ion powder with average particle size of 1-10 mu m and specific surface area of 150m2(ii) in terms of/g. The comminution is carried out in a high-speed comminution mechanical impact mill at 1000 rpm for 3 minutes.
The obtained porous calcium silicate-loaded rare earth ion filler powder is subjected to dispersion loading through porous calcium silicate, the average particle size of the filler powder is 5 mu m, and the specific surface area is 160m2The mass ratio of the rare earth ion component to the active calcium silicate is 15 percent.
Example 2 of embodiment
1) Preparing a soluble precursor of a rare earth component into impregnation liquid in water according to a weight ratio, wherein the rare earth ion component is in the form of lanthanum or cerium oxide or carboxylate; cerium oxide with a ratio of rare earth component to active calcium silicate of 30% when a double rare earth ionic component is used, the ratio of the two metal elements lanthanum and cerium is 1: 2;
2) the porous calcium silicate is prepared by hydrothermal synthesis, the average particle size of the porous calcium silicate is 5 mu m, and the specific surface area of the porous calcium silicate is 170m2(ii) in terms of/g. Refining the porous calcium silicate raw material by a grinding and stripping machine; the stirring speed is 500 r/min, the grinding and peeling time is 1 hour, and the content of the suspension during grinding and peeling is 20 percent.
3) Mixing the porous calcium silicate suspension with the rare earth component impregnation liquid, adjusting the pH value of the system to 10, uniformly stirring, and adjusting the pH value to obtain an alkaline substance which is ammonia water; after the reaction is finished, directly carrying out spray drying or drying and roasting after filtering and washing, wherein the addition amount of the dispersing agent is 1.0 percent of the weight of the porous calcium silicate, the dispersing agent is sodium stearate, the mixing and stirring time of the porous calcium silicate suspension and the impregnation liquid is 5 minutes, the mixing and stirring temperature is 30 ℃, the stirring speed is 400 r/m, the stirring time is 0.5 hour, and the solid content of the suspension is 15 percent. The rare earth soluble precursor is lanthanum nitrate, and the temperature of spray drying is 360 ℃; the drying temperature is 110 ℃, the roasting temperature is 400 ℃, and the roasting time is 2 hours.
4) Finally, after crushing and scattering, porous calcium silicate loaded rare earth ion powder is obtained, the average particle size is 6 mu m, and the specific surface area is 190m2(ii) in terms of/g. The comminution is carried out in a high-speed comminution mechanical impact mill at 1000 rpm for 6 minutes.
The obtained porous calcium silicate-loaded rare earth ion filler powder is subjected to dispersion loading through porous calcium silicate, the average particle size of the filler powder is 6 mu m, and the specific surface area is 190m2The mass ratio of the rare earth ion component to the active calcium silicate is 25 percent.
EXAMPLE 3
1) Preparing a soluble precursor of a rare earth component into impregnation liquid in water according to a weight ratio, wherein the rare earth ion component is in the form of lanthanum or cerium oxide or carboxylate; lanthanum oxide with a rare earth component to active calcium silicate ratio of 30% when a double rare earth ionic component is used, the ratio of the two metal elements lanthanum and cerium is 2: 1;
2) the porous calcium silicate is prepared by hydrothermal synthesis, the average particle size of the porous calcium silicate is 5 mu m, and the specific surface area is 270m2(ii) in terms of/g. Refining the porous calcium silicate raw material by a grinding and stripping machine; the stirring speed is 1500 rpm, the grinding and peeling time is 2 hours, and the content of the suspension during grinding and peeling is 35 percent.
3) Mixing the porous calcium silicate suspension with the rare earth component impregnation liquid, adjusting the pH value of the system to 11, uniformly stirring, and adjusting the pH value to obtain an alkaline substance tetraethylammonium hydroxide; after the reaction is finished, directly carrying out spray drying or drying and roasting after filtering and washing, wherein the addition amount of the dispersing agent is 1.0 percent of the weight of the porous calcium silicate; the dispersing agent is sodium hexametaphosphate, the mixing and stirring time of the porous calcium silicate suspension and the impregnation liquid is 5 minutes, the mixing and stirring temperature is 30 ℃, the stirring speed is 500 r/min, the stirring time is 1 hour, and the solid content of the suspension is 25 percent. The rare earth soluble precursor is ammonium ceric nitrate, and the temperature of spray drying is 450 ℃; the drying temperature is 120 ℃, the roasting temperature is 450 ℃, and the roasting time is 4 hours.
4) Finally, after crushing and scattering, porous calcium silicate loaded rare earth ion powder is obtained, the average particle size is 10 mu m, and the specific surface area is 200m2(ii) in terms of/g. The pulverization and breaking are carried out in a mechanical impact mill with high-speed pulverization at 4000 rpm for 10 minutes.
The obtained porous calcium silicate-loaded rare earth ion filler powder is subjected to dispersion loading through porous calcium silicate, the average particle size of the filler powder is 10 mu m, and the specific surface area is 200m2The mass ratio of the rare earth ion component to the active calcium silicate is 30 percent.
The porous calcium silicate is artificially synthesized by a hydrothermal method, has the characteristics of low density, large specific surface area and the like, is a fluffy porous structural inorganic material with aggregates, has the characteristics of void development in the particle and honeycomb aggregate appearance, has high adsorption property to powder due to the pore effect, light base effect, nano effect and strong light base holding capacity of the particles, and can improve and enhance the processing property, mechanical property, flame retardant property and the like of a polymer composite material product by using the inorganic reinforced filler as a non-petroleum base green functional inorganic reinforced filler; meanwhile, the large specific surface area of the porous calcium silicate can also provide a good carrier environment for various active components.
Although the embodiments of the present invention have been described above, the above descriptions are only for the convenience of understanding the present invention, and are not intended to limit the present invention. It will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims.
Claims (10)
1. The preparation method of the porous calcium silicate rare earth ion-loaded filler powder is characterized by comprising the following steps:
1) adding water and a dispersing agent into a porous calcium silicate raw material according to a weight ratio to prepare a suspension;
2) preparing a soluble precursor of a rare earth component into impregnation liquid in water according to a weight ratio, wherein the rare earth ion component is in a lanthanum or cerium compound form, and the compound form is an oxide or carboxylate form; the proportion of the rare earth component and the active calcium silicate is 1.5 to 30 percent; when the double rare earth ion component is adopted, the ratio of two metal elements, namely lanthanum and cerium, is 2: 1 to 1: 2;
3) mixing the porous calcium silicate suspension with the rare earth component impregnation liquid, adjusting the pH value of the system to 8-11, and uniformly stirring; after the reaction is finished, directly carrying out spray drying or drying and roasting after filtering and washing;
4) finally, after crushing and scattering, obtaining porous calcium silicate loaded rare earth ion powder with the average particle size of 1-10 mu m and the specific surface area of 150-200 m2/g。
2. The method for preparing the porous calcium silicate rare earth ion-loaded filler powder according to claim 1, wherein the porous calcium silicate is prepared by hydrothermal synthesis, the average particle size of the porous calcium silicate is 1-5 μm, and the specific surface area of the porous calcium silicate is 170-300 m2/g。
3. The preparation method of the porous calcium silicate rare earth ion-loaded filler powder according to claim 1, characterized in that the porous calcium silicate raw material in the step 1) is refined by a mill-stripper; the stirring speed is 400-1500 rpm, the grinding and peeling time is 1-2 hours, and the content of the suspension during grinding and peeling is 15-35%.
4. The porous calcium silicate rare earth ion-loaded filler powder and the preparation method thereof according to claim 1, wherein the addition amount of the dispersant in the step 1) is 0.5-1.5% of the weight of the porous calcium silicate, and the preferable addition ratio is 0.5-1.0% of the porous calcium silicate; the dispersing agent is one of sodium polyacrylate, sodium stearate and sodium hexametaphosphate; the stirring speed is 400-500 rpm, the stirring time is 0.5-1 hour, and the solid content of the suspension is 15-25%.
5. The method for preparing the porous calcium silicate rare earth ion-loaded filler powder according to claim 1, wherein the rare earth soluble precursor in the step 2) is one or more of lanthanum nitrate hydrate, lanthanum chloride, cerium nitrate hexahydrate and ammonium cerium nitrate; the mass fraction of the impregnation liquid is 1-10%.
6. The method for preparing the porous calcium silicate rare earth ion-loaded filler powder according to claim 1, wherein the alkaline substance for regulating the pH value in the step 3) is one of ammonia water, tetraethylammonium hydroxide or tetramethylammonium hydroxide, and preferably the alkaline substance is ammonia water.
7. The method for preparing the porous calcium silicate rare earth ion-loaded filler powder according to claim 1, wherein the mixing and stirring time of the porous calcium silicate suspension and the impregnation liquid in the step 3) is 5-40 minutes, and the mixing and stirring temperature is 30-75 ℃.
8. The method for preparing the porous calcium silicate rare earth ion-loaded filler powder according to claim 1, wherein the temperature of the spray drying in the step 3) is 350-450 ℃; the drying temperature is 105-120 ℃, the roasting temperature is 350-450 ℃, and the roasting time is 2-4 hours.
9. The method for preparing the porous calcium silicate rare earth ion-loaded filler powder according to claim 1, wherein the pulverization and scattering in the step 4) are performed in a high-speed pulverizer, a scattering machine or a high-speed mechanical impact mill at 1000 rpm to 4500 rpm for 1 minute to 10 minutes.
10. The filler powder of porous calcium silicate loaded rare earth ions is characterized in that the filler powder is dispersed and loaded through porous calcium silicate, the average particle size of the filler powder is 1-10 mu m, and the specific surface area of the filler powder is 150-200 m2The mass ratio of the rare earth ion component to the active calcium silicate is 1 to 30 percent.
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