CN1597527A - Preparation method low electric conductiving super fine aluminium hydroxide micro powder - Google Patents
Preparation method low electric conductiving super fine aluminium hydroxide micro powder Download PDFInfo
- Publication number
- CN1597527A CN1597527A CN 200410049908 CN200410049908A CN1597527A CN 1597527 A CN1597527 A CN 1597527A CN 200410049908 CN200410049908 CN 200410049908 CN 200410049908 A CN200410049908 A CN 200410049908A CN 1597527 A CN1597527 A CN 1597527A
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- China
- Prior art keywords
- aluminium hydroxide
- crystal seed
- ultrafine aluminium
- low conductivity
- preparation
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- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 title claims abstract description 32
- 229910021502 aluminium hydroxide Inorganic materials 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims description 8
- 239000000843 powder Substances 0.000 title abstract description 3
- 239000013078 crystal Substances 0.000 claims abstract description 16
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910001388 sodium aluminate Inorganic materials 0.000 claims abstract description 11
- 238000005406 washing Methods 0.000 claims abstract description 10
- 238000001914 filtration Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 19
- 239000003595 mist Substances 0.000 claims description 19
- 239000012065 filter cake Substances 0.000 claims description 9
- 239000005432 seston Substances 0.000 claims description 6
- 239000003513 alkali Substances 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 3
- 239000006210 lotion Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 9
- 239000000047 product Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 229910001679 gibbsite Inorganic materials 0.000 description 5
- 238000000354 decomposition reaction Methods 0.000 description 4
- 239000012153 distilled water Substances 0.000 description 4
- 239000003063 flame retardant Substances 0.000 description 4
- 239000002585 base Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000009881 electrostatic interaction Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000011157 advanced composite material Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000012815 thermoplastic material Substances 0.000 description 1
Landscapes
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
A process for preparing superfine aluminium hydroxide powder with low electric conductivity includes such steps as desiliconizing the solution of sodium aluminate, adding crystal seeds, decomposing, filtering, washing the filtered cake, refiltering, and baking.
Description
Technical field
A kind of preparation method of low conductivity ultrafine aluminium hydroxide relates to the preparation method as a kind of low conductivity aluminium hydroxide powder of fire retardant, insulating material.
Background technology
The ultrafine aluminium hydroxide micro mist is superfine because of its particle, and have fire-retardant, eliminate smoke and fill three big functions, in advanced composite materialss such as plastics, rubber, add this product, it is fire-retardant from breath, smoke elimination performance that product is had, and resist electric leakage, anti-electric arc, wear resisting property to strengthen, being widely used in industries such as cable, insulator, thermoplastic materials, electric apparatus equipment, plastics, rubber and making compound, is the fire retardant of the nuisanceless environment-friendly type of generally acknowledging in the world, and very big consumption is arranged every year.Because ultrafine aluminium hydroxide micro mist granularity is superfine, specific surface area is bigger, high adsorption capacity, makes the solvable ionogen in the aqueous solution be adsorbed on its surface, the physical index specific conductivity is at 230-340 μ s/cm, and there is electrostatic interaction on the micro mist surface, and shows polarity.Poor with organic consistency, thereby cause when in macromolecular materials such as resin, adding a large amount of filling material viscosity to increase easily, make poor processability, dispersed bad, and be easy to generate electrical breakdown, limited ultrafine aluminium hydroxide micro mist add-on, and in insulativity requires than higher organic polymer material, can't use.
Summary of the invention
The objective of the invention is the deficiency that exists in the above-mentioned prior art, provide a kind of reduction micro mist of effectively, realizing easily conductivity indices, improve the ultrafine aluminium hydroxide micro mist use properties, widen the low conductivity ultrafine aluminium hydroxide micropowder preparing process of its purposes.
The objective of the invention is to be achieved through the following technical solutions.
A kind of low conductivity ultrafine aluminium hydroxide micropowder preparing process, the employing sodium aluminate solution is a raw material, it is characterized in that preparation process is followed successively by: with sodium aluminate solution carry out desiliconization purify to siliceous modulus more than 600, seston less than 0.02% after, adding crystal seed coefficient is that the kind of 3%-12% is divided crystal seed, under 50 ℃ of-73 ℃ of temperature, decompose after 3-8 hour, filter; With the washing of in stirring washing trough, pulling an oar of filtering ultrafine aluminium hydroxide micro mist filter cake, be lower than 0.05g/L until last washing lotion total alkali content in NaO, refilter oven dry.
A kind of low conductivity ultrafine aluminium hydroxide micropowder preparing process is characterized in that: the crystal seed that adds in the preparation process is the D through the surface active of mechanical mill
50Active aluminium hydroxide crystal seed at 0.4-3 μ m.
A kind of low conductivity ultrafine aluminium hydroxide micropowder preparing process is characterized in that: filter back filter cake moisture content weight content less than 30%.
Method of the present invention can be utilized same granularity active seed, controls different decomposition technique conditions, obtains D
50It in the crystalline form of 0.4-3 μ m the ultrafine aluminium hydroxide micro mist of α-gibbsite.Can produce the ultrafine aluminium hydroxide micro mist of different grain size brand.
Method of the present invention, the employing industrial sodium aluminate solution is a raw material, adds special active aluminium hydroxide with low temperature and stirs the process system that decomposes.Its feature is used low-temperature decomposition, is added the decomposition technique of active seed, and static state adopts the pure water washing with stirring to wash.Make the micro mist surface adsorb the solubility ionogen less; And be strict controlled in 30% filtering filter cake moisture content, the dissolubility ionogen is taken away with water, improve the quality of products.
Method of the present invention purifies sodium aluminate solution and carries out desiliconization and purify and reach 600 to siliceous modulus and get final product, in theory with put into practice the siliceous modulus height and will help the quality product raising, but too high index request can increase production cost greatly, causes unreasonable economically.
Preparation low conductivity ultrafine aluminium hydroxide micro mist of the present invention, specific conductivity has effectively been improved the electrostatic interaction of micro mist than being lower than traditional 180-110 μ s/cm, has improved its processing characteristics, improves and widen the Application Areas of ultrafine aluminium hydroxide micro mist greatly.
Description of drawings
Fig. 1 is a kind of process flow sheet of low conductivity ultrafine aluminium hydroxide micropowder preparing process.
Specific embodiments
Below in conjunction with example method of the present invention is described further.
A kind of low conductivity ultrafine aluminium hydroxide micropowder preparing process, the sodium aluminate solution that employing purifies through three desiliconizations, siliceous modulus is more than 600, seston is less than 0.02%, controlled temperature is at 50 ℃ of-73 ℃ of degree, and adding grinds the active seed that is equipped with through machinery, and the crystal seed coefficient is 3%-12%, stable control decomposition temperature is decomposed at 50 ℃-73 ℃, and the resolving time is 3-8 hour.It is the ultrafine aluminium hydroxide micro mist of α-gibbsite in the crystalline form of 0.4-3 μ m that filtration washing adopts the static washing of distilled water to obtain D50, and slurries refilter and obtain filter cake moisture content below 30% and strengthen oven dry.The Granularity Distribution of producing with present method is even, and crystallization is perfect, and specific conductivity is low, improves ultrafine aluminium hydroxide micro mist and organic macromolecule consistency, improves the insulating property of product.
Embodiment 1
Sodium aluminate solution is carried out desiliconization to be purified, siliceous modulus is 700, seston is 0.02%, under 54 ℃ of temperature, adding crystal seed coefficient is 10% the active seed through mechanical mill, and controlled temperature is to decompose under 55 ℃, decomposes and washs after 3 hours, adopt distilled water wash to count 0.05g/L to containing full alkali concn NaO, be filtered to the filter cake weight in wet base and be 30% strengthen oven dry again, break up, classification.The product that obtains is that D50 is the ultrafine aluminium hydroxide micro mist of α-gibbsite at the crystal formation of 0.5-0.7 μ m, and resistivity is 140 μ S/cm.
Embodiment 2
Sodium aluminate solution is carried out desiliconization to be purified, siliceous modulus is 650, seston is 0.02%, under 61 ℃ of temperature, adding crystal seed coefficient is 4% the active seed through mechanical mill, and controlled temperature is to decompose under 61 ℃, decomposes and washs after 5 hours, adopt distilled water wash to count 0.05g/L to containing full alkali concn NaO, be filtered to the filter cake weight in wet base and be 25% strengthen oven dry again, break up, classification.The product that obtains is that D50 is the ultrafine aluminium hydroxide micro mist of α-gibbsite at the crystal formation of 0.7-1.0 μ m, and resistivity is 110 μ S/cm.
Embodiment 3
Sodium aluminate solution is carried out desiliconization to be purified, siliceous modulus is 640, seston is 0.02%, under 68 ℃ of temperature, adding crystal seed coefficient is 12% the active seed through mechanical mill, and controlled temperature is to decompose under 68 ℃, decomposes and washs after 6 hours, adopt distilled water wash to count 0.05g/L to containing full alkali concn NaO, be filtered to the filter cake weight in wet base and be 24% strengthen oven dry again, break up, classification.The product that obtains is that D50 is the ultrafine aluminium hydroxide micro mist of α-gibbsite at the crystal formation of 1.2-1.8 μ m, and resistivity is 90 μ S/cm.
Claims (3)
1. low conductivity ultrafine aluminium hydroxide micropowder preparing process, the employing sodium aluminate solution is a raw material, it is characterized in that preparation process is followed successively by: with sodium aluminate solution carry out desiliconization purify to siliceous modulus more than 600, seston less than 0.02% after, adding crystal seed coefficient is that the kind of 3%-12% is divided crystal seed, under 50 ℃ of-73 ℃ of temperature, decompose after 3-8 hour, filter; With the washing of in stirring washing trough, pulling an oar of filtering ultrafine aluminium hydroxide micro mist filter cake, be lower than 0.05g/L until last washing lotion total alkali content in NaO, refilter oven dry.
2. according to the described a kind of low conductivity ultrafine aluminium hydroxide micropowder preparing process of root claim 1, it is characterized in that: the crystal seed that adds in the preparation process is through the D50 of the surface active of the mechanical mill active aluminium hydroxide crystal seed at 0.4-3 μ m.
3. according to the described a kind of low conductivity ultrafine aluminium hydroxide micropowder preparing process of root claim 1, it is characterized in that: filter back filter cake moisture content weight content less than 30%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410049908 CN1278938C (en) | 2004-06-18 | 2004-06-18 | Preparation method low electric conductiving super fine aluminium hydroxide micro powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410049908 CN1278938C (en) | 2004-06-18 | 2004-06-18 | Preparation method low electric conductiving super fine aluminium hydroxide micro powder |
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| Publication Number | Publication Date |
|---|---|
| CN1597527A true CN1597527A (en) | 2005-03-23 |
| CN1278938C CN1278938C (en) | 2006-10-11 |
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| CN 200410049908 Active CN1278938C (en) | 2004-06-18 | 2004-06-18 | Preparation method low electric conductiving super fine aluminium hydroxide micro powder |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100411990C (en) * | 2006-01-23 | 2008-08-20 | 中国铝业股份有限公司 | Method for preparing aluminium hydroxide micropowder |
| CN102336425A (en) * | 2011-08-04 | 2012-02-01 | 中国铝业股份有限公司 | Method for preparing aluminum hydroxide micro-powder with low oil absorption rate |
| CN102502731A (en) * | 2011-10-13 | 2012-06-20 | 河津市晋铝大株化工有限公司 | Method for manufacturing superfine aluminum hydroxide micropowder |
| CN102515224A (en) * | 2011-12-14 | 2012-06-27 | 河津市晋铝大株化工有限公司 | Method for producing aluminum hydroxide powder |
| CN104045100A (en) * | 2014-06-27 | 2014-09-17 | 中国铝业股份有限公司 | Preparation method of aluminum hydroxide |
| CN104749724A (en) * | 2015-04-03 | 2015-07-01 | 江苏南方通信科技有限公司 | Novel high-flame-retardance optical fiber filling paste and preparation method |
| CN105776269A (en) * | 2016-03-24 | 2016-07-20 | 中国铝业股份有限公司 | Micro-powder aluminum hydroxide preparation method and device and micro-powder aluminum hydroxide |
| CN106986362A (en) * | 2017-04-12 | 2017-07-28 | 柳健康 | A kind of sodium aluminate solution high concentration is low admittedly containing one section of seeded precipitation technique |
| CN110372021A (en) * | 2019-06-13 | 2019-10-25 | 山东泰星新材料股份有限公司 | A kind of preparation method and application of electronic circuit board or electrician's fire retardant aluminium hydroxide |
| CN112028095A (en) * | 2020-08-12 | 2020-12-04 | 中铝山东有限公司 | Superfine aluminum hydroxide seed crystal and preparation method thereof, submicron aluminum hydroxide and preparation method and application thereof |
-
2004
- 2004-06-18 CN CN 200410049908 patent/CN1278938C/en active Active
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100411990C (en) * | 2006-01-23 | 2008-08-20 | 中国铝业股份有限公司 | Method for preparing aluminium hydroxide micropowder |
| CN102336425A (en) * | 2011-08-04 | 2012-02-01 | 中国铝业股份有限公司 | Method for preparing aluminum hydroxide micro-powder with low oil absorption rate |
| CN102502731A (en) * | 2011-10-13 | 2012-06-20 | 河津市晋铝大株化工有限公司 | Method for manufacturing superfine aluminum hydroxide micropowder |
| CN102515224A (en) * | 2011-12-14 | 2012-06-27 | 河津市晋铝大株化工有限公司 | Method for producing aluminum hydroxide powder |
| CN104045100A (en) * | 2014-06-27 | 2014-09-17 | 中国铝业股份有限公司 | Preparation method of aluminum hydroxide |
| CN104749724A (en) * | 2015-04-03 | 2015-07-01 | 江苏南方通信科技有限公司 | Novel high-flame-retardance optical fiber filling paste and preparation method |
| CN104749724B (en) * | 2015-04-03 | 2017-09-12 | 江苏南方通信科技有限公司 | A kind of new high flame retardant optical fiber filling paste and preparation method thereof |
| CN105776269A (en) * | 2016-03-24 | 2016-07-20 | 中国铝业股份有限公司 | Micro-powder aluminum hydroxide preparation method and device and micro-powder aluminum hydroxide |
| CN106986362A (en) * | 2017-04-12 | 2017-07-28 | 柳健康 | A kind of sodium aluminate solution high concentration is low admittedly containing one section of seeded precipitation technique |
| CN110372021A (en) * | 2019-06-13 | 2019-10-25 | 山东泰星新材料股份有限公司 | A kind of preparation method and application of electronic circuit board or electrician's fire retardant aluminium hydroxide |
| CN112028095A (en) * | 2020-08-12 | 2020-12-04 | 中铝山东有限公司 | Superfine aluminum hydroxide seed crystal and preparation method thereof, submicron aluminum hydroxide and preparation method and application thereof |
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| Publication number | Publication date |
|---|---|
| CN1278938C (en) | 2006-10-11 |
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