CN1513761A - Preparation method of nano-level magnesium hydroxide - Google Patents
Preparation method of nano-level magnesium hydroxide Download PDFInfo
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- CN1513761A CN1513761A CNA021601461A CN02160146A CN1513761A CN 1513761 A CN1513761 A CN 1513761A CN A021601461 A CNA021601461 A CN A021601461A CN 02160146 A CN02160146 A CN 02160146A CN 1513761 A CN1513761 A CN 1513761A
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Abstract
A process for preparing magnesium hydroxide nanoparticles by reverse deposition method features that the solution of magnesium salt is used as its raw material, the sodium hydroxide and ammonia water are used as mixed precipitant, and the crystal growth mechanism is used to control the granularity. Its advantages are simple equipment, high purity, low cost and (30-100)-nm diameter.
Description
Technical field
The present invention relates to a kind of preparation method's of magnesium hydroxide, particularly nanometric magnesium hydroxide preparation method.
Background technology
Magnesium hydroxide be a kind of addition type have a filling, fire-retardant and press down the inorganic combustion inhibitor of cigarette triple functions, can be used for the fire-retardant of multiple polymers.In addition, magnesium hydroxide also can be used for flue gas desulfurization in the environmental protection, processing lead waste water and waste water and takes off ammonium dephosphorization etc., and pressing down the application that all has aspect cigarette coating and biology and the pharmaceutical preparation in various degree at acid rain soil remediation, food and fodder additives, oil dope, agricultural fertiliser containing magnesium, cigarette tissue, is a kind of generally acknowledged environment amenable green chemical industry product.
The preparation method of magnesium hydroxide has a variety of, but have a production meaning mainly contain three kinds of technologies (see " inorganic chemicals industry handbook second edition, volume two, p1050～1054 page), promptly synthesis method, rhombspar are selected calcination method and electrolysis bittern method.Wherein rhombspar selection calcination method only is used for the production to the not high magnesium hydroxide of purity requirement, and the energy consumption of electrolysis bittern method is too high, and application limit is very big.Therefore, using maximum production technique at present is chemical synthesis, wherein representative synthesis technique (is seen " inorganic chemical product ", the Si Tujiesheng chief editor, the p320 page or leaf) is bittern-lime method, bittern-ammoniacal liquor method and magnesia-hydrochloric acid-ammoniacal liquor method, but there are many weak points in these technologies: or gel phenomenon is arranged, and the precipitation particles tiny gel phenomenon of healing is more serious, causes very big difficulty for the filtration washing of product; Or the pH value of system is wayward, and the yield of product is low; Or product is prone to the secondary aggregation phenomenon in precipitation, filtration procedure, finally can't obtain the nano level superfine particle.
At present, about nanometric magnesium hydroxide preparation method invention disclosed patent has following several: CN1332116A adopts solubility magnesium salts and alkali, synthesize the magnesium hydroxide of median size between 10～200nm by the homogeneous fluid method through forcing precipitin reaction, this technology is simple, convenient, but the size distribution broad of gained magnesium hydroxide, and say on the stricti jurise that the particle diameter that surpasses 100nm has not belonged to nanoparticle; CN1341694A utilizes purified magnesium chloride solution that old bittern or magnesite obtains and industrial ammonia or ammonia to be raw material, perhaps utilize Adlerika and industrial ammonia or ammonia to be raw material, adopt hypergravity (rotating packed bed) technology, utilize liquid-liquid phase reaction or gas-liquid phase reaction mode, the magnesium hydroxide of preparation median size between 35～90nm, be characterized in that technical process is simple, grain diameter is even, but need specific equipment-rotating packed bed (hypergravity), facility investment is relatively large; CN1356361A is a raw material with natural brucite or sintered magnesia, prepares the magnesium hydroxide of median size below 100nm through case of wet attrition, and this method is the simplest, but can only the not high magnesium hydroxide of production purity requirement; CN1361062A is that the coprecipitation reaction that the full back-mixing liquid film reactor of employing liquid-liquid two-phase coprecipitation reaction carries out magnesium salts and alkali lye prepares the magnesium hydroxide of median size between 62～92nm, this method technology is close with CN1341694A, gained magnesium hydroxide particle size distribution is even, but the processing charges costliness (gap of rotor and stator must be controlled at 1～20 μ m) of required specific equipment-full back-mixing liquid film reactor, equipment are difficult to safeguard.
In sum, the existing special specific equipment of method need that prepare high-purity nano level magnesium hydroxide particles is invested greatlyyer, and the Operation and Maintenance expense is higher.
Summary of the invention
The object of the invention provides that a kind of investment is less, the method for preparing nanometric magnesium hydroxide that the Operation and Maintenance expense is lower.
The method that supplies to prepare nanometric magnesium hydroxide that the present invention carries, be to utilize that crystal generates, growth mechanism control particle size, the employing magnesium salt solution is a raw material, with sodium hydroxide and ammoniacal liquor as mixed precipitant, prepare nanometric magnesium hydroxide by the reverse precipitator method, detailed process is as follows:
1. magnesium salts is mixed with the aqueous solution of certain mass concentration, it is standby to be heated to certain temperature;
2. be mixed with the mixed precipitant of certain pH value with sodium hydroxide, ammoniacal liquor and water, it is standby to be heated to certain temperature;
3. be mixed with finite concentration mass concentration aqueous ethanolic solution, control standby at a certain temperature:
4. magnesium salt solution is added in the mixed precipitant rapidly under high degree of agitation and be carried out to nuclear reaction;
5. after filtration washing,, vacuum-drying promptly get nanometric magnesium hydroxide.
Above-mentioned magnesium salt solution can be magnesium chloride or magnesium nitrate, and concentration is 5～13%, and Heating temperature can be 40～80 ℃.
The pH value of above-mentioned mixed precipitant is greater than 10, and Heating temperature can be 40～80 ℃.
Above-mentioned one-tenth nuclear reaction is under high degree of agitation, rapidly magnesium chloride (or magnesium nitrate) aqueous solution added in the mixed precipitant, and reaction 1～30min, under ultrasonic concussion in the impouring aqueous ethanolic solution, keeping 10～120min time is 1～30min then.
The mass concentration of above-mentioned aqueous ethanolic solution is 50～90%, and temperature is controlled at-10～20 ℃.
If magnesium hydroxide needs surface modification, sodium stearate (or anion surfactant, silane coupling agent) sodium stearate or anion surfactant, silane coupling agent can be dissolved in the aqueous ethanolic solution.
In the process of prepared nanometric magnesium hydroxide provided by the invention, with magnesium chloride (or magnesium nitrate) solution under high degree of agitation in the reverse adding mixed precipitant, so both can make crystal nucleation react moment and finish, also be convenient to the accurate control of system pH.With above-mentioned reaction solution under ultrasonic concussion in the reverse impouring cold ethanol aqueous solution, make full use of the difference of magnesium hydroxide solubleness in the different properties medium, further strengthened the crystal nucleation reaction, the effect of ultrasonic concussion in addition can be avoided growing up and agglomeration of nanoparticle to greatest extent.The intervention of alcohol component in the system not only can be eliminated gel phenomenon fully, and the filtration washing of product is become carry out easily.
Utilize prepared nanometric magnesium hydroxide provided by the invention, technology is simple, convenient and easy, need not specific installation, to invest for a short time, and processing parameter is convenient to control, and the purity of products obtained therefrom surpasses 99%, and grain diameter is generally between 30～100nm.
Embodiment
Embodiment 1
At first, with magnesium chloride (MgCl
26H
2O) 50.8g dissolves in the 345g water, is mixed with the magnesium chloride brine of mass concentration about 6%, be heated to 80 ℃ standby; Other gets concentration is 25～28% ammoniacal liquor 30ml and 90g water mixing, and the sodium hydroxide solution with 40% is adjusted pH ≈ 14, be heated to 70 ℃ standby; The preparation mass concentration is 90% aqueous ethanolic solution 150ml, and with its temperature reduce to-8 ℃ standby.Then, under high degree of agitation, rapidly magnesium chloride brine is added in the mixed precipitant, behind the reaction 20min, under ultrasonic concussion, in the impouring aqueous ethanolic solution, keep low temperature 30min, at last after filtration, washing, vacuum-drying promptly get magnesium hydroxide.Laser particle analyzer records the product cut size scope between 30～80nm, and it is 99.9% that median size 68nm, elemental microanalysis method record its purity.
Embodiment 2
At first, with magnesium chloride (MgCl
26H
2O) 50.8g dissolves in the 132g water, is mixed with the magnesium chloride brine of mass concentration about 13%, be heated to 80 ℃ standby; Other gets concentration is 25～28% ammoniacal liquor 40ml and 200g water mixing, and the sodium hydroxide solution with 40% is adjusted pH ≈ 13, be heated to 60 ℃ standby; The preparation mass concentration is 60% aqueous ethanolic solution 200ml, and with its temperature reduce to 5 ℃ standby.Then, under high degree of agitation, rapidly magnesium chloride brine is added in the mixed precipitant, behind the reaction 10min, under ultrasonic concussion, in the impouring aqueous ethanolic solution, keep low temperature 30min, at last after filtration, washing, vacuum-drying promptly get magnesium hydroxide.Laser particle analyzer records the product cut size scope between 30～100nm, and it is 99.2% that median size 76nm, elemental microanalysis method record its purity.
Embodiment 3
At first, with magnesium chloride (MgCl
26H
2O) 50.8g dissolves in the 187g water, is mixed with the magnesium chloride brine of mass concentration about 10%, be heated to 80 ℃ standby; Other gets concentration is 25～28% ammoniacal liquor 48ml and 150g water mixing, and the sodium hydroxide solution with 40% is adjusted pH ≈ 11, be heated to 50 ℃ standby; The preparation mass concentration is 70% aqueous ethanolic solution 180ml, and with its temperature reduce to-2 ℃ standby.Then, under high degree of agitation, rapidly magnesium chloride brine is added in the mixed precipitant, behind the reaction 3min, under ultrasonic concussion, in the impouring aqueous ethanolic solution, keep low temperature 30min, at last after filtration, washing, vacuum-drying promptly get magnesium hydroxide.Laser particle analyzer records the product cut size scope between 40～95nm, and it is 99.3% that median size 72nm, elemental microanalysis method record its purity.
Embodiment 4
At first, with magnesium nitrate [Mg (NO
3)
26H
2O] 128.2g dissolves in the 613g water, is mixed with the magnesium chloride brine of mass concentration about 10%, be heated to 80 ℃ standby; Other gets concentration is 25～28% ammoniacal liquor 45ml and 100g water mixing, and the sodium hydroxide solution with 40% is adjusted pH＞14, be heated to 60 ℃ standby; The preparation mass concentration is 80% aqueous ethanolic solution 200ml, and with its temperature reduce to-5 ℃ standby.Then, under high degree of agitation, rapidly magnesium nitrate aqueous solution is added in the mixed precipitant, behind the reaction 10min, under ultrasonic concussion, in the impouring aqueous ethanolic solution, keep low temperature 30min, at last after filtration, washing, vacuum-drying promptly get magnesium hydroxide.Laser particle analyzer records the product cut size scope between 30～90nm, and it is 99.1% that median size 54nm, elemental microanalysis method record its purity.
Claims (9)
1, the invention provides a kind of preparation method of nanometric magnesium hydroxide, it is characterized in that utilizing crystal generation, growth mechanism control particle size, the employing magnesium salt solution is a raw material, with sodium hydroxide and ammoniacal liquor as mixed precipitant, prepare nanometric magnesium hydroxide by the reverse precipitator method, detailed process is as follows:
1. magnesium salts is mixed with the aqueous solution of certain mass concentration, it is standby to be heated to certain temperature;
2. be mixed with the mixed precipitant of certain pH value with sodium hydroxide, ammoniacal liquor and water, it is standby to be heated to certain temperature;
3. prepare the certain mass concentration ethanol aqueous solution, control standby at a certain temperature;
4. magnesium salt solution is added in the mixed precipitant rapidly under high degree of agitation and be carried out to nuclear reaction;
5. after filtration washing,, vacuum-drying promptly get nanometric magnesium hydroxide.
2,, it is characterized in that described magnesium salt solution concentration is 5～13% according to the preparation method of claim 1.
3,, it is characterized in that described magnesium salt solution is magnesium chloride or magnesium nitrate according to the preparation method of claim 1.
4,, it is characterized in that described magnesium salt solution temperature is 40～80 ℃ according to the preparation method of claim 1.
5, according to the preparation method of claim 1, the pH value that it is characterized in that described mixed precipitant is greater than 10, and temperature is 40～80 ℃.
6,, it is characterized in that the described nucleation reaction times is 1～30min according to the preparation method of claim 1.
7,, it is characterized in that described reaction solution is in the reverse impouring cold ethanol aqueous solution, to keep 10～120min under ultrasonic concussion, with further reinforcement crystal nucleation reaction according to the preparation method of claim 1.
8, according to the preparation method of claim 1, the mass concentration that it is characterized in that described aqueous ethanolic solution is 50～90%, and temperature is controlled at-10～20 ℃.
9,, it is characterized in that described sodium stearate or anion surfactant, silane coupling agent being dissolved in the aqueous ethanolic solution according to the preparation method of claim 1.
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| CN 02160146 CN1255321C (en) | 2002-12-31 | 2002-12-31 | Preparation method of nano-level magnesium hydroxide |
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| CN 02160146 CN1255321C (en) | 2002-12-31 | 2002-12-31 | Preparation method of nano-level magnesium hydroxide |
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| CN1513761A true CN1513761A (en) | 2004-07-21 |
| CN1255321C CN1255321C (en) | 2006-05-10 |
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Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1295270C (en) * | 2005-02-23 | 2007-01-17 | 杨第伦 | Process for preparing magnesium hydroxide loose nano blocked flame retardant and products therefrom |
| CN100506695C (en) * | 2007-07-27 | 2009-07-01 | 中国铝业股份有限公司 | Method for synthesizing flame retardant of magnesium hydroxide |
| CN101173115B (en) * | 2007-10-27 | 2010-06-02 | 太原理工大学 | Ultra-fine magnesium hydroxide surface modifying method |
| US7736485B2 (en) | 2006-08-11 | 2010-06-15 | Aqua Resources Corporation | Nanoplatelet magnesium hydroxides and methods of preparing same |
| CN101857249A (en) * | 2010-06-23 | 2010-10-13 | 华东理工大学 | Preparation method of magnesium hydroxide |
| CN102060314A (en) * | 2010-11-30 | 2011-05-18 | 沈阳鑫劲粉体工程有限责任公司 | Preparation method for synthesizing platy flame-retardant magnesium hydroxide by using light burned magnesia powder |
| CN102502728A (en) * | 2011-10-12 | 2012-06-20 | 江苏艾特克阻燃材料有限公司 | Magnesium hydroxide flame retardant and preparation method thereof |
| CN102849761A (en) * | 2012-09-30 | 2013-01-02 | 河北工业大学 | Preparation method of magnesium hydrate |
| CN104193615A (en) * | 2014-05-16 | 2014-12-10 | 江苏大学 | Catalytic oxidation method for 1,2-propanediol |
| WO2015089777A1 (en) * | 2013-12-18 | 2015-06-25 | 中国科学院福建物质结构研究所 | Method for preparing light, ball-flower shaped nanometer magnesium hydroxide with high specific surface area |
| CN105968687A (en) * | 2016-05-25 | 2016-09-28 | 张小雨 | Electromagnetic shielding plastic and manufacturing technique thereof |
| US9604854B2 (en) | 2006-08-11 | 2017-03-28 | Aqua Resources Corporation | Nanoplatelet metal oxides |
| CN108529654A (en) * | 2018-05-07 | 2018-09-14 | 天津君瑞和科技有限公司 | A method of with making from brine for micro/nano level magnesium hydroxide |
| CN110240184A (en) * | 2019-05-25 | 2019-09-17 | 邢台镁熙环保材料有限公司 | A kind of production technology of high-purity Nano-class magnesia |
-
2002
- 2002-12-31 CN CN 02160146 patent/CN1255321C/en not_active Expired - Fee Related
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1295270C (en) * | 2005-02-23 | 2007-01-17 | 杨第伦 | Process for preparing magnesium hydroxide loose nano blocked flame retardant and products therefrom |
| US7736485B2 (en) | 2006-08-11 | 2010-06-15 | Aqua Resources Corporation | Nanoplatelet magnesium hydroxides and methods of preparing same |
| US7892447B2 (en) | 2006-08-11 | 2011-02-22 | Aqua Resources Corporation | Nanoplatelet metal hydroxides and methods of preparing same |
| US10273163B2 (en) | 2006-08-11 | 2019-04-30 | Aqua Resources Corporation | Nanoplatelet metal oxides |
| US9604854B2 (en) | 2006-08-11 | 2017-03-28 | Aqua Resources Corporation | Nanoplatelet metal oxides |
| CN100506695C (en) * | 2007-07-27 | 2009-07-01 | 中国铝业股份有限公司 | Method for synthesizing flame retardant of magnesium hydroxide |
| CN101173115B (en) * | 2007-10-27 | 2010-06-02 | 太原理工大学 | Ultra-fine magnesium hydroxide surface modifying method |
| CN101857249A (en) * | 2010-06-23 | 2010-10-13 | 华东理工大学 | Preparation method of magnesium hydroxide |
| CN102060314B (en) * | 2010-11-30 | 2012-06-20 | 沈阳鑫劲粉体工程有限责任公司 | Preparation method for synthesizing platy flame-retardant magnesium hydroxide by using light burned magnesia powder |
| CN102060314A (en) * | 2010-11-30 | 2011-05-18 | 沈阳鑫劲粉体工程有限责任公司 | Preparation method for synthesizing platy flame-retardant magnesium hydroxide by using light burned magnesia powder |
| CN102502728B (en) * | 2011-10-12 | 2014-07-23 | 江苏艾特克阻燃材料有限公司 | Magnesium hydroxide flame retardant and preparation method thereof |
| CN102502728A (en) * | 2011-10-12 | 2012-06-20 | 江苏艾特克阻燃材料有限公司 | Magnesium hydroxide flame retardant and preparation method thereof |
| CN102849761A (en) * | 2012-09-30 | 2013-01-02 | 河北工业大学 | Preparation method of magnesium hydrate |
| WO2015089777A1 (en) * | 2013-12-18 | 2015-06-25 | 中国科学院福建物质结构研究所 | Method for preparing light, ball-flower shaped nanometer magnesium hydroxide with high specific surface area |
| CN104193615A (en) * | 2014-05-16 | 2014-12-10 | 江苏大学 | Catalytic oxidation method for 1,2-propanediol |
| CN105968687A (en) * | 2016-05-25 | 2016-09-28 | 张小雨 | Electromagnetic shielding plastic and manufacturing technique thereof |
| CN108529654A (en) * | 2018-05-07 | 2018-09-14 | 天津君瑞和科技有限公司 | A method of with making from brine for micro/nano level magnesium hydroxide |
| CN110240184A (en) * | 2019-05-25 | 2019-09-17 | 邢台镁熙环保材料有限公司 | A kind of production technology of high-purity Nano-class magnesia |
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| CN1255321C (en) | 2006-05-10 |
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