CN1113922A - Porous oxide micro-balls with uniform granule size and preparing method - Google Patents
Porous oxide micro-balls with uniform granule size and preparing method Download PDFInfo
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- CN1113922A CN1113922A CN 94105909 CN94105909A CN1113922A CN 1113922 A CN1113922 A CN 1113922A CN 94105909 CN94105909 CN 94105909 CN 94105909 A CN94105909 A CN 94105909A CN 1113922 A CN1113922 A CN 1113922A
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Abstract
The present invention utilizes the stacked silicon beads method combining with the method of stopping technology in midway to make the refractory oxide colloidal particles their grain size is 1-500 nm stack into the resultant porous microballs of oxide with particle diameter of 0.1-20 micro m., mainly 1-10 micro m and 85%-90% of particle diameter distributing in the range of minus or plus 0.1D (D being average particle diameter). Said invention overcame the complex operating technology in the production course, the productive method is simple, the products are highly uniform and can be used as efficient catalyst carrier and efficient adsorhent and are specially suitable for using as the matrix of high efficient liquid phase chromatographic fixed phase.
Description
The present invention relates to a kind of particle diameter uniform oxide porous microsphere, oxide porous microballoon of particularly narrow distribution and preparation method thereof.
Porous oxides can be used as toughener, additive or the sorbent material of carrier, macromolecular material and tensio-active agent etc. of matrix, the effective catalyst of liquid chromatography stationary phase as silicon-dioxide, zirconium dioxide, titanium dioxide, aluminium sesquioxide etc.Wherein, silicon-dioxide, zirconium dioxide, titanium dioxide, aluminium sesquioxide are widely used in respectively on the matrix of high performance liquid chromatography stationary phase or in the research that remains to be developed the matrix that becomes the high performance liquid chromatography stationary phase.
The advantage that the porous oxides microballoon is used for effective catalyst is: the porous oxides microballoon has higher specific surface area, is used for can improving the contact area of catalyzer behind the carrier of catalyzer, thereby improves catalytic efficiency.
The porous oxides microballoon, the advantage that is used for high performance liquid chromatography stationary phase matrix as silicon-dioxide is: (1) has higher physical strength and rigidity, can realize the purpose of high performance liquid chromatography; (2) particle diameter is controlled, can obtain the little and uniform particle of particle diameter; (3) controllable aperture; (4) easy bonding can be widely used in preparing various types of chromatographic stationary phases.In addition, zirconium dioxide, aluminium sesquioxide, titanium dioxide etc. have superior resistance to acids and bases, have the more satisfactory outstanding advantage that becomes widely used chromatographic stationary phase matrix.
At present in the world, because multinomial needs such as HPLC and efficient catalytics, the production of porousness microballoons such as silica gel is developed widely, has formed four, 50 patents about the porasil microballoon since nineteen sixty-five.According to its know-why difference, they can be divided three classes: (1) stacked silica bead method; (2) SOL-GEL method; (3) spray-drying process.But product or the particle diameter produced are inhomogeneous, or size distribution is wide, complex process.As the public clear 60-71516 of spy, Ger.Pat.2, the disadvantage that the SOL-GEL legal system of disclosures such as 357,184 is equipped with the silica gel technology is that particle diameter is extremely inhomogeneous, must relate to complicated particle grading technology.Special for another example public clear 62-275,104, in the spray drying method for preparation silica gel technology that discloses such as special public clear 62-143818, the size distribution heterogeneity of products obtained therefrom also must relate to complicated particle grading technology.
U.S. Pat Pat.3782075(1974) and US Pat.3,855,172(1974) have confidential relation with the present invention, in these two patents, disclosed the stacked silica bead ratio juris.Though the product of producing, size distribution is more superior than other method, and the size distribution of 90% particle is (D is the particle diameter of product, and for the product of 5 μ, 90% particle distribution is in the scope of ± 2.5 μ) in the particle size range of 0.5D-1.5D.The present invention utilizes the stacked silica bead ratio juris, in conjunction with the processing method of ending, produces the size distribution porous microsphere of uniform oxide more midway.
The homogeneity of chromatograph packing material is very important to the meaning of high performance liquid chromatography, and at first, chromatograph packing material can bring lower post to press to chromatographic column uniformly; Secondly, uneven chromatograph packing material can bring the broadening effect of chromatographic peak, reduces the resolving power of chromatographic separation.Just can obtain chromatograph packing material matrix the most uniformly by the present invention, thereby obtain chromatograph packing material the most uniformly.
The objective of the invention is to overcome size distribution heterogeneity in the existing porous microsphere technology of preparing, the shortcoming of particle fractionation of complex technology, need be through complicated technology, prepare the porous microsphere of highly even and narrow diameter distribution, to be applicable to the needs of liquid chromatography stationary phase matrix, efficient catalytic agent carrier and high-efficiency adsorbent etc.
The present invention utilizes the stacked silica bead method in conjunction with ending size distribution that explained hereafter the goes out 85-90% porous oxides microballoon in ± 0.1D scope midway.Product of the present invention is piled up by the colloidal particle of the littler oxide compound of particle diameter and is formed, and its aperture is by the particle diameter decision of colloid microballon, and its pore volume is made of the accumulation hole between these colloid microballons.
The stacked silica bead ratio juris is: after allowing to form the colloidal solution uniform mixing of the polymer monomer that is insoluble to polymerization system and resistivity against fire oxide compound, add polymerizing catalyst, initiated polymerization is to form polymer precipitation, thereby destroy the stability of colloid system, make colloidal particle with the polymkeric substance sedimentation, formed polymer precipitation exists with the polymer spherical particle, thereby obtains containing the polymer spherical particle of the colloidal inorganic particle of oxide compound.Because there is hydroxyl in the colloidal particle surface, with the method for high-temperature firing, in the process of the organic constituent in removing this spheroidal particle, between the hydroxyl on colloidal particle surface dehydration reaction takes place, thereby colloidal particle is bonded together, obtained the porous microsphere of resistivity against fire oxide compound.
The present invention selects for use formaldehyde and urea element for causing the settled polymer monomer of colloidal inorganic particle.This polymerization system reaction times is subjected to the concentration affects of polymerization temperature and polymerizing catalyst.When increasing respectively, polymerization temperature and catalyst concn all can increase the speed of response of this polymerization system.This polyreaction is condensation reaction, remove catalyzer after, polyreaction stops immediately.After selecting suitable polymerizing condition, the beginning of particle growth and intermediate stage in polymerization process, the particle diameter of polymer particle evenly increases, and homogeneity is fabulous; And,, thereby caused the ununiformity of polymerisate particle because newborn particle can not get enough monomers and supply with in polymerization latter stage.Therefore proceed to a certain intermediate stage in polymerization, end the carrying out of polyreaction, just can obtain a series of particle diameter differences and the oxide porous microballoon of the uniform resistivity against fire of size distribution height.
When selecting for use formaldehyde and melamine to be polymer monomer, the middle processing method of ending of using the present invention to propose also can obtain the uniform porous oxides microballoon of particle diameter.
Preparation method of the present invention:
(1) at temperature of reaction 2-100 ℃, under the best 5-40 ℃ of temperature, with 0.8: 1-4: the 1(mol ratio), be preferably 1: 1-2: the plain mixing solutions of 1 formaldehyde and urea, joining concentration is 0.1-30%, particle diameter is in the 1-500nm(nanometer), be preferably in the self-control or commercially available oxide colloid liquid of 7-150nm, making oxide colloid is 0.1 with the ratio of urea element: 1-10: the 1(mol ratio);
(2) in step (1), add the strongly-acid material and make catalyzer, make and cause the acid range pH=1-5 of formaldehyde with the urea element, best pH=1-3, reaction times is 0.1-24 hour, the polymkeric substance that is generated bonds together resistivity against fire oxide colloid particle and forms the microspheroidal product, along with the increase of time, the particle diameter of spherical products increases;
(3) before formaldehyde and plain 100% conversion of urea, add basic solution in the system of step (2), neutralization is acid, pH value=5-10; Polyreaction is ended;
(4) separate as the described reaction product of step (3), remove unreacted reactant, the cleaning, drying product;
(5) at the product of 400-700 ℃ of sintering step (4), obtaining particle diameter is 0.1-20 μ m, and the size distribution of 85-90% is at the oxide porous microballoon of ± 0.1D.
The employed strongly-acid material of production technique of the present invention comprises hydrochloric acid, sulfuric acid, phosphoric acid, nitric acid, acetic acid etc., and all can be mineral acid or the organic acid of regulating arbitrarily between the 1-6 at pH.The employed alkaline matter of production technique of the present invention comprises all alkaline matters, as sodium oxide, potassium oxide, Lithium Oxide 98min, calcium oxide, magnesium oxide, sodium hydroxide, potassium hydroxide, lithium hydroxide, calcium hydroxide, sodium phosphate, primary amine, secondary amine, tertiary amines etc. are regulated neutral model titanium oxide colloid, ferric oxide colloid, antimonous oxide colloid, tindioxide colloid or their mixture colloid used.Oxide porous microballoon is the porous microsphere of silicon-dioxide, aluminium sesquioxide, zirconium dioxide, titanium dioxide, ferric oxide, antimonous oxide, tindioxide or their mixture.
In each stage of preparation method's step (3), by add the termination agent of polyreaction in different steps, can obtain a series of particle diameter is 0.1-20 μ m, mainly is 1-10 μ m, and the particle diameter uniform oxide porous microsphere of the size distribution of 85-90% in ± 0.1D scope.
With the porous oxide microballoon that production of the present invention obtains, have 85%～90% size distribution high homogeneity and the withstand voltage 200-500Kg/cm of reaching in ± 0.1D scope
2Characteristics, specific pore volume is at 1.3-1.5cm
3Between/the g, the aperture all is suitable for the needs of efficient liquid phase chromatographic stuffing matrix, efficient catalytic agent carrier and high-efficiency adsorbent etc. between 20-4000A °.The uniform characteristics of its particle diameter height make it be particularly suitable for being used as the matrix of efficient liquid phase chromatographic stuffing.
Embodiment 1
Get 10 gram silicon sol (concentration is 30%, and the median size of colloidal particle is 8nm) and be diluted to 1 premium on currency solution, add plain 6.0 grams of urea, formaldehyde 11.1 grams (concentration is 36%) mix.When temperature is 20 ℃, add catalyzer-HCL, the pH that makes reaction system is 2.0.React after 40 minutes, add NaOH and make the pH of system be increased to 7, reaction terminating.Separation, drying products are in the specific pore volume 1.35cm of 500 ℃ of silica obtained products of sintering
3/ g, aperture 100A °, particle diameter 2 μ m, size distribution: 85～90% be distributed in ± scope of 0.2 μ m in, the withstand voltage 400Kg/cm that reaches
2
Embodiment 2
Get 30 gram silicon sol (concentration is 30%, and the median size of colloidal particle is 20nm) and be diluted to 1 premium on currency solution, add plain 18.0 grams of urea, formaldehyde 33.3 grams (concentration is 36%) mix.When temperature is 20 ℃, add catalyzer-HCL, the pH that makes reaction system is 2.0.React after 70 minutes, add NaOH and make the pH of system be increased to 8, reaction terminating.Separate drying products, in 500 ℃ of sintering.The specific pore volume 1.4cm of silica obtained product
3/ g, aperture 150A °, particle diameter 5 μ m, size distribution: 85%～90% be distributed in ± scope of 0.3 μ m in, the withstand voltage 500Kg/cm that reaches
2
Embodiment 3
Get 100 gram silicon sol (concentration is 30%, and the median size of colloidal particle is 100nm) and be diluted to 1 premium on currency solution, add plain 30.0 grams of urea, formaldehyde 70.0 grams (concentration is 36%) mix.When temperature is 40 ℃, add catalyzer-HCL, the pH that makes reaction system is 2.0.React after 30 minutes, add NH
4OH makes the pH of system be increased to 6, reaction terminating.Separation, drying products are in the specific pore volume 1.3cm of 500 ℃ of silica obtained products of sintering
3/ g, aperture 400A °, particle diameter 4 μ m, size distribution: 85%～90% be distributed in ± scope of 0.3 μ m in.
Embodiment 4
Get 80 gram zirconium colloidal sols (concentration is 7%, and the median size of colloidal particle is 50nm) and be diluted to 1 premium on currency solution, add plain 6.0 grams of urea, formaldehyde 20.0 grams (concentration is 36%) mix.When temperature is 20 ℃, add catalyzer-HCL, the pH that makes reaction system is 1.7.React after 30 minutes, add NH
4OH makes the pH of system be increased to 6, reaction terminating.Separation, drying products are in 550 ℃ of sintering.The specific pore volume 1.3cm of many zirconiums of gained ball product
3/ g, aperture 80A °, particle diameter 4 μ m, size distribution: 85%～90% be distributed in ± scope of 0.4 μ m in.
Embodiment 5
Get 50 gram titanium colloidal sols (concentration is 10%, and the median size of colloidal particle is 10nm) and be diluted to 1 premium on currency solution, add plain 6.0 grams of urea, formaldehyde 12.0 grams (concentration is 36%) mix.When temperature is 28 ℃, add catalyzer-H
2SO
4, the pH that makes reaction system is 2.2.React after 60 minutes, add NH
4OH makes the pH of system be increased to 6, reaction terminating.Separation, drying products are in the specific pore volume 1.33cm of 550 ℃ of silica obtained products of sintering
3/ g, aperture 80A °, particle diameter 4 μ m, size distribution: 85%～90% be distributed in ± scope of 0.5 μ m in.
Claims (8)
1, a kind of oxide porous microballoon is characterized in that particle diameter is 0.1-20 μ m, mainly is 1-10 μ m, and the size distribution of 85%-90% is at the oxide porous microballoon of ± 0.1D (D is a median size).
2, oxide porous microballoon as claimed in claim 1 is characterized in that described oxide compound is silicon-dioxide, aluminium sesquioxide, zirconium dioxide, titanium dioxide, ferric oxide, antimonous oxide, tindioxide or their mixture.
3, a kind of preparation method of oxide porous microballoon is characterized in that:
(1) under temperature of reaction 2-100 ℃, with 0.8: 1-4: the formaldehyde 1(mol ratio) is with the mixing solutions of urea element, joining concentration is 0.1-30%, and particle diameter is the 1-500nm(nanometer) oxide colloid liquid in, making oxide colloid is 0.1 with the ratio of urea element: 1-10: the 1(mol ratio);
(2) add the strongly-acid material in step (1) and make catalyzer, making initiation formaldehyde is pH=1-5 with the acidity of urea element, and the reaction times is 0.1-24 hour, forms spherical products;
(3) before formaldehyde and plain 100% conversion of urea, add basic solution in the system of step (2), neutralization is acid, and pH=5-10 ends polyreaction;
(4) separate product, remove unreacted reactant as reaction as described in the step (3), the cleaning, drying product,
(5) at the product of 400-700 ℃ of sintering step (4), obtaining particle diameter is 0.1-20 μ m, and the size distribution of 85%-90% is at the porous microsphere of ± 0.1D.
4, the preparation method of oxide porous microballoon as claimed in claim 3 is characterized in that described oxide colloid is silicon dioxide colloid, aluminium sesquioxide colloid, zirconium dioxide colloid, colloidal tio 2, ferric oxide colloid, antimonous oxide colloid, tindioxide colloid or their mixture colloid.
5, the preparation method of oxide porous microballoon as claimed in claim 3 is characterized in that described temperature of reaction, and the best is 5-40 ℃.
6, the preparation method of oxide porous microballoon as claimed in claim 3 is characterized in that described initiation formaldehyde is pH=1-3 with the acid optimum range of urea element.
7, the preparation method of oxide porous microballoon as claimed in claim 3 is characterized in that described oxide colloid particle optimum grain-diameter is the 7-150nm(nanometer).
8, the preparation method of oxide porous microballoon as claimed in claim 3 is characterized in that described formaldehyde is 1 with the best proportioning of the mixing solutions of urea element: 1-2: 1.
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| Application Number | Priority Date | Filing Date | Title |
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| CN94105909A CN1048998C (en) | 1994-06-02 | 1994-06-02 | Porous oxide micro-balls with uniform granule size and preparing method |
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| CN94105909A CN1048998C (en) | 1994-06-02 | 1994-06-02 | Porous oxide micro-balls with uniform granule size and preparing method |
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| CN1113922A true CN1113922A (en) | 1995-12-27 |
| CN1048998C CN1048998C (en) | 2000-02-02 |
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| CN94105909A Expired - Fee Related CN1048998C (en) | 1994-06-02 | 1994-06-02 | Porous oxide micro-balls with uniform granule size and preparing method |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010121488A1 (en) * | 2009-04-21 | 2010-10-28 | 河北勇龙邦大新材料有限公司 | Method and device for producing hollow microspheres |
| CN103708510A (en) * | 2012-09-28 | 2014-04-09 | 同济大学 | Preparation method of layered alumina microspheres |
| CN104185607A (en) * | 2011-12-22 | 2014-12-03 | 加巴国际控股有限公司 | Processes for the preparation of stannic oxide |
| CN108467057A (en) * | 2018-06-29 | 2018-08-31 | 佛山腾鲤新能源科技有限公司 | A kind of preparation method of porous nano stannous oxide |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1041529C (en) * | 1992-04-29 | 1999-01-06 | 武汉地质管理干部学院 | Process for refining and bleaching barite powder |
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1994
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010121488A1 (en) * | 2009-04-21 | 2010-10-28 | 河北勇龙邦大新材料有限公司 | Method and device for producing hollow microspheres |
| US8845936B2 (en) | 2009-04-21 | 2014-09-30 | Hebei Yl-Bangda New Materials Limited Company | Process and device for the preparation of hollow microspheres comprising centrifugal atomization |
| EA020857B1 (en) * | 2009-04-21 | 2015-02-27 | Хэбэй Ил-Банда Нью Матириалз Лимитед Компани | Method for producing hollow microspheres |
| CN104185607A (en) * | 2011-12-22 | 2014-12-03 | 加巴国际控股有限公司 | Processes for the preparation of stannic oxide |
| CN103708510A (en) * | 2012-09-28 | 2014-04-09 | 同济大学 | Preparation method of layered alumina microspheres |
| CN103708510B (en) * | 2012-09-28 | 2016-01-20 | 同济大学 | A kind of preparation method of stratiform aluminum oxide micro-sphere |
| CN108467057A (en) * | 2018-06-29 | 2018-08-31 | 佛山腾鲤新能源科技有限公司 | A kind of preparation method of porous nano stannous oxide |
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| CN1048998C (en) | 2000-02-02 |
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