CN102992366A - Process method for preparing aluminum hydroxide micropowder - Google Patents

Process method for preparing aluminum hydroxide micropowder Download PDF

Info

Publication number
CN102992366A
CN102992366A CN201210467079XA CN201210467079A CN102992366A CN 102992366 A CN102992366 A CN 102992366A CN 201210467079X A CN201210467079X A CN 201210467079XA CN 201210467079 A CN201210467079 A CN 201210467079A CN 102992366 A CN102992366 A CN 102992366A
Authority
CN
China
Prior art keywords
aluminum hydroxide
seed
sodium aluminate
aluminate solution
hydroxide powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201210467079XA
Other languages
Chinese (zh)
Inventor
林齐
李桂兰
苏向东
黄健
李勇
高贵龙
范文波
丁元法
熊永昇
李鹏
陈向东
罗宏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NEW-MATERIAL RESEARCH AND DEVELOPMENT BASE GUIZHOU PROV
Original Assignee
NEW-MATERIAL RESEARCH AND DEVELOPMENT BASE GUIZHOU PROV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NEW-MATERIAL RESEARCH AND DEVELOPMENT BASE GUIZHOU PROV filed Critical NEW-MATERIAL RESEARCH AND DEVELOPMENT BASE GUIZHOU PROV
Priority to CN201210467079XA priority Critical patent/CN102992366A/en
Publication of CN102992366A publication Critical patent/CN102992366A/en
Pending legal-status Critical Current

Links

Abstract

The invention discloses a process method for preparing aluminum hydroxide micropowder and belongs to a method for preparing the aluminum hydroxide micropowder. In the method, the seed crystal dosage is small, the cost is low, and the product granularity is controllable. The method comprises the following steps of: adding active seed crystals with the weight being 0.01-0.05 time that of a sodium aluminate solution in the sodium aluminate solution, and uniformly stirring for 6-8 hours under the temperature being 50-80 DEG C so as to obtain seed slurry, wherein the active seed crystals are the aluminum hydroxide micropowder with the granularity being 3.6-8.3 micrometers and the Na2O content being 0.3-1%; mixing the seed slurry with the sodium aluminate solution, so as to obtain a mixed solution, wherein the seed slurry accounts for 0.1-0.5% the weight of the mixed solution; and stirring the mixed solution by using a micro-disturbance plug flow crystallization reactor under the temperature being 40-80 DEG C for 8-48 hours, and collecting crystallized aluminum hydroxide micropowder. The aluminum hydroxide micropowder prepared by using the method has the advantages of being low in cost, fine in particles, high in grade and the like.

Description

The fine aluminum hydroxide powder process of preparing
Technical field
The present invention relates to a kind of method for preparing fine aluminum hydroxide powder, relate in particular to a kind of method of utilizing the sodium aluminate solution reaction decomposes to prepare fine aluminum hydroxide powder.
Background technology:Fine aluminum hydroxide powder is widely used in the industries such as fire-retardant and filler.Its preparation method mainly contains three kinds at present: a kind of is that technical grade volume particle size aluminium hydroxide is carried out the physics fragmentation, and obtaining granularity is the product of 5-20 μ m; Two kinds be directly take fine aluminum hydroxide powder as seed and sodium aluminate solution reaction directly decompose and produce fine aluminum hydroxide powder, the method requires the fine aluminum hydroxide powder grain weight large, the fine aluminum hydroxide powder particle size range of output is wide, thickness is inhomogeneous; Three kinds is to adopt various acid (wherein also comprising carbonic acid gas) and sodium aluminate solution neutralization reaction to generate aluminium glue, and then the aging fine aluminum hydroxide powder seed that generates is produced fine aluminum hydroxide powder with this seed and sodium aluminate solution reaction decomposes again; This technique digestion time is long, need take large measuring tank tank, energy-output ratio is large, and production of hybrid seeds neutralization reaction is brought a large amount of acid group impurity to Sodium Aluminate Solution System.
Summary of the invention:For the defects that exists in the prior art, the present invention aims to provide the fine aluminum hydroxide powder process of preparing that a kind of amount of seed is few, cost is low, product granularity is controlled.
To achieve these goals, the present invention is by the following technical solutions:
1) add the active seed of 0.01~0.05 times of weight in sodium aluminate solution, uniform stirring is 6~8 hours under 50~80 ℃ of conditions, gets the seed slurry; Described active seed is that granularity is 3.6~8.3 μ m, Na 2O content is 0.3~1% fine aluminum hydroxide powder, and the alumina content in the described sodium aluminate solution is 120~150 grams per liters;
2) above-mentioned seed slurry is mixed with above-mentioned sodium aluminate solution, get mixed solution; Under 40~80 ℃ of conditions, stir this mixed solution 8~48 hours with the moving plug flow crystallization reactor of perturbation, collect the fine aluminum hydroxide powder of crystallization; Wherein, the seed slurry accounts for 0.1~0.5% of described mixed solution weight.
Compared with the prior art, the present invention is owing to having adopted two-step approach to prepare fine aluminum hydroxide powder, and utilized the moving plug flow crystallization reactor of perturbation to control reaction process, therefore can control decomposition aluminium hydroxide form out by the liquid flow pattern of controlling in this reactor, thereby produce satisfactory crystal morphology.Moreover, the seed of the fine aluminum hydroxide powder that the inventive method adopts (fine aluminum hydroxide powder) consumption only adds 1/10th (the conventional aluminum acid sodium solution adds 0.1~0.5 times of weight that the required seed of crystal seed reaction method for preparing is sodium aluminate solution) of the required seed of crystal seed reaction method for preparing for the conventional aluminum acid sodium solution, cost is low; Prepared fine aluminum hydroxide powder granularity can reach 0.5~5 μ m, and product hierarchy is high.
Embodiment:The invention will be further described below in conjunction with specific embodiment:
Embodiment 1
1) 0.05 times heavy of adding, granularity are the active seed of 8.3 μ m in sodium aluminate solution, and uniform stirring is 6 hours under 80 ℃ temperature, gets the seed slurry;
2) get sodium aluminate solution 999Kg and mix with above-mentioned seed slurry 1Kg, stirred 8 hours under 40 ℃ temperature with the moving plug flow crystallization reactor of perturbation, can collect the fine aluminum hydroxide powder that mean particle size is 0.58 μ m; This fine aluminum hydroxide powder is the hexagonal plate crystal.
Embodiment 2
1) 0.01 times heavy of adding, granularity are the active seed of 3.6 μ m in sodium aluminate solution, and uniform stirring is 8 hours under 50 ℃ temperature, gets the seed slurry;
2) get sodium aluminate solution 995Kg and mix with above-mentioned seed slurry 5Kg, stirred 48 hours under 80 ℃ temperature with the moving plug flow crystallization reactor of perturbation, can collect the fine aluminum hydroxide powder that mean particle size is 4.8 μ m; This fine aluminum hydroxide powder is hexagonal prismoid shape crystal.
In the various embodiments described above, the alumina content in the sodium aluminate solution is 120~150 grams per liters, and described active seed is Na 2O content is 0.3~1% fine aluminum hydroxide powder.

Claims (1)

1. fine aluminum hydroxide powder process of preparing is characterized in that method is as follows:
1) add the active seed of 0.01~0.05 times of weight in sodium aluminate solution, uniform stirring is 6~8 hours under 50~80 ℃ of conditions, gets the seed slurry; Described active seed is that granularity is 3.6~8.3 μ m, Na 2O content is 0.3~1% fine aluminum hydroxide powder, and the alumina content in the described sodium aluminate solution is 120~150 grams per liters;
2) above-mentioned seed slurry is mixed with above-mentioned sodium aluminate solution, get mixed solution; Under 40~80 ℃ of conditions, stir this mixed solution 8~48 hours with the moving plug flow crystallization reactor of perturbation, collect the fine aluminum hydroxide powder of crystallization; Wherein, the seed slurry accounts for 0.1~0.5% of described mixed solution weight.
CN201210467079XA 2012-11-19 2012-11-19 Process method for preparing aluminum hydroxide micropowder Pending CN102992366A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210467079XA CN102992366A (en) 2012-11-19 2012-11-19 Process method for preparing aluminum hydroxide micropowder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210467079XA CN102992366A (en) 2012-11-19 2012-11-19 Process method for preparing aluminum hydroxide micropowder

Publications (1)

Publication Number Publication Date
CN102992366A true CN102992366A (en) 2013-03-27

Family

ID=47921573

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210467079XA Pending CN102992366A (en) 2012-11-19 2012-11-19 Process method for preparing aluminum hydroxide micropowder

Country Status (1)

Country Link
CN (1) CN102992366A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104671266A (en) * 2013-11-28 2015-06-03 北京阳光欣禾科技有限公司 Process for preparing ultrafine aluminum hydroxide by seed crystal precipitation method
CN104817100A (en) * 2015-04-15 2015-08-05 中南大学 Method for preparing sand-shaped aluminum oxide

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20080082751A (en) * 2007-03-09 2008-09-12 케이씨 주식회사 Manufacturing method of ultra fine aluminum hydroxide
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
CN102583474A (en) * 2012-01-20 2012-07-18 贵州省新材料研究开发基地 Process method for producing aluminum hydroxide by seed decomposition of supersaturated sodium aluminate solution

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20080082751A (en) * 2007-03-09 2008-09-12 케이씨 주식회사 Manufacturing method of ultra fine aluminum hydroxide
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
CN102583474A (en) * 2012-01-20 2012-07-18 贵州省新材料研究开发基地 Process method for producing aluminum hydroxide by seed decomposition of supersaturated sodium aluminate solution

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
《轻金属》 20021231 林齐等 "二段中分发生产超细氢氧化铝微粉" 第15-17页 1 , 第10期 *
林齐等: ""二段中分发生产超细氢氧化铝微粉"", 《轻金属》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104671266A (en) * 2013-11-28 2015-06-03 北京阳光欣禾科技有限公司 Process for preparing ultrafine aluminum hydroxide by seed crystal precipitation method
CN104817100A (en) * 2015-04-15 2015-08-05 中南大学 Method for preparing sand-shaped aluminum oxide

Similar Documents

Publication Publication Date Title
CN103232044B (en) Synthesis method of nanoscale MCM-49 (Multi Chip Module) molecular sieve
CN102432027B (en) Monodisperse large-grain-diameter and high-stability acid silica sol and preparation method thereof
CN102211779B (en) Method for preparing beta zeolite
CN102491395A (en) Preparation method of nano-grade calcium carbonate
CN104743573A (en) ZSM-5 molecular sieve and preparation method thereof
CN102757075B (en) Method for preparing calcium carbonate powders of different structures and shapes
CN102030348B (en) Device and method for continuously preparing magnesium hydroxide flame retardant
CN109437261A (en) A kind of sheeted nanometer magnesium hydroxide raw powder's production technology
CN104478699A (en) Preparation method of high-purity superfine cobalt oxalate powder
CN105293516A (en) Method for rapidly preparing ZSM-22 molecular sieve by means of seed crystal
CN101863496A (en) Method for preparing battery grade lithium carbonate by purifying industrial grade lithium carbonate
CN102992366A (en) Process method for preparing aluminum hydroxide micropowder
CN103601210B (en) Wilkinite one step alkali is fused into the method for zeolite
WO2014005498A1 (en) Method for preparing aluminum dihydrogen tripolyphosphate
CN102107880A (en) Method for preparing zeolite 4A
CN102618093A (en) Clay composite material and preparation method thereof
CN101781796A (en) Simple method for preparing hydroxyapatite nanocrystals
CN111302347B (en) Preparation method of high-purity large-particle-size silica sol
CN101580293A (en) Decolorization method for sodium aluminate solution
CN101863492A (en) Synthesis method of 4A-type zeolite
CN109694085B (en) Template-free synthesis method of ammonium type ZSM-5 nanosheet
CN107758687B (en) Synthesis method of disk-shaped mordenite with different thicknesses
CN202968150U (en) Device combination for preparing superfine molybdenum trioxide
CN102351207B (en) Method for preparing nano attapulgite by solvothermal process
CN102070167B (en) Production method of monocrystalline aluminum hydroxide

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20130327