CN1072392A - The preparation method of cubic crystal antimony trioxide - Google Patents
The preparation method of cubic crystal antimony trioxide Download PDFInfo
- Publication number
- CN1072392A CN1072392A CN 92114236 CN92114236A CN1072392A CN 1072392 A CN1072392 A CN 1072392A CN 92114236 CN92114236 CN 92114236 CN 92114236 A CN92114236 A CN 92114236A CN 1072392 A CN1072392 A CN 1072392A
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- China
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- antimony
- tartrate
- butter
- antimony trioxide
- cubic crystal
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G30/00—Compounds of antimony
- C01G30/004—Oxides; Hydroxides; Oxyacids
- C01G30/005—Oxides
Abstract
A kind of preparation method of cubic crystal antimony trioxide ties up in the alkaline aqueous solution butter of antimony solution direct hydrolysis, obtains cubic crystal antimony trioxide through washing and oven dry.Characteristics of the present invention are to adopt in the hydrolysis reaction tartrate or tartrate as coordination agent, and the mol ratio of butter of antimony and tartrate or tartrate is 1-26: 1.The method reaction times of the present invention is short, and easy and simple to handle, gained cubic crystal antimony trioxide complete in crystal formation is single, the purity height, and color and luster is good, is the good catalyst of production of polyester.Present method can be used for the scale operation cubic crystal antimony trioxide.
Description
The present invention relates to a kind of preparation method of metal oxide, more particularly, is about the preparation method as the cubic crystal antimony trioxide of production of polyester catalyzer.
Antimonous oxide has two kinds of crystal existence forms, and a kind of is that cubic system is a senarmontite, and another kind is that rhomboidal crystal is an antimony bloom.Because the difference of their crystalline structure, their molecular property also has difference in some aspects, as on catalytic activity as the production of polyester catalyzer, the catalytic activity of cubic crystal antimony trioxide is significantly better than the catalytic activity of rhomboidal crystal antimonous oxide, and the photostabilization of cubic crystal antimony trioxide is better than the photostabilization of rhomboidal crystal antimonous oxide.
Prepare in the method for antimonous oxide, two kinds of pyrogenic process and wet methods are arranged.The antimonous oxide of pyrogenic process production mostly is the mixture of cubic system and rhomboidal crystal.Impurity such as high price sb oxide appear in equipment complexity that pyrogenic process is produced easily.Japanese Patent JP79,108,798 and JP80,114,418 relate to the preparation method of single cubic crystal antimonous oxide, this method is metallic antimony and lead to be mixed in by a certain percentage carry out oxidation in the smelting furnace, constantly adds metallic antimony and simultaneously the cubic crystal antimony trioxide that generates is blown out collection by airflow line.
French Patent Fr.2,488,259 relate to a kind of method that butter of antimony solution direct hydrolysis is obtained single cubic crystal antimonous oxide in alkaline medium, but must there be a kind of oxygenant such as hydrogen peroxide to exist in the hydrolysis medium, the consumption of oxygenant (in contrast to the weight of butter of antimony) between 0.4-5%, hydrolysis temperature is at 0-100 ℃, and PH carries out between the 7-12.Equally, in order to prevent the generation of high price sb oxide and amorphous antimonous oxide, hydrolysis operational condition complexity, the butter of antimony strength of solution is lower, and hydrolysis time is longer.
Russian patent SU1,065,344 relates to and a kind ofly adds industrial antimonous oxide form the antimony oxalate subsalt with it in oxalic acid solution, decompose the method that obtains cubic crystal antimony trioxide then, but consumption of oxalic acid is big, cost is high, long reaction time, and product forms colloid, is difficult for washing.
The preparation method who the purpose of this invention is to provide the single cubic crystal antimonous oxide that a kind of reaction times is short, simple to operate, purity is high, efficient is high.
Method of the present invention is included in the alkaline medium butter of antimony solution direct hydrolysis, through steps such as washing, oven dry, obtains cubic crystal antimony trioxide.Concrete grammar is as follows:
Water and hydrochloric acid are deployed into the butter of antimony solution that proportion is 1.5-2.5 with the butter of antimony solid, under agitation butter of antimony solution is joined in the alkaline aqueous solution that contains the coordination agent with katalysis, coordination agent can be tartrate, sodium tartrate, ammonium tartrate, and the present invention has certain requirement to the consumption of coordination agent.Because coordination agent is limited to the coordination ability of antimony ion, if the consumption of coordination agent is too little, then the part antimony ion can hydrolysis generate the rhomboidal crystal antimonous oxide, and hydrolysis reaction obtains the mixture of cubic crystal antimony trioxide and rhomboidal crystal antimonous oxide at last; If the consumption of coordination agent is too big, because the coordination agent consumption is big, cause waste on the one hand, cost is improved, can make the throw out washing time lengthening of hydrolysis on the other hand.In the present invention, the mol ratio of butter of antimony and coordination agent can be 1-26: 1, be more preferably 15-26: 1.Alkaline aqueous solution can be ammoniacal liquor or aqueous sodium carbonate.As use strong aqua, then the volume of ammoniacal liquor be the butter of antimony liquor capacity 1.5-3.0 doubly, to guarantee that the solution behind the hydrolysis reaction serves as neutral to alkalescence, if ammonia volume very little, solution slant acidity behind the hydrolysis reaction, then hydrolysis reaction generates antimony oxychloride.Hydrolysis reaction does not have special requirement to temperature, and reaction can be carried out between 10-80 ℃, and at room temperature reaction gets final product generally speaking.Hydrolysis reaction generally promptly reacted completely through stirring in 10-30 minute.The antimonous oxide sedimentation speed that hydrolysis reaction generates is fast, and available decantation washing then 100-160 ℃ of oven dry, promptly obtains single cubic crystalline antimonous oxide.
The antimonous oxide of present method preparation is 100% cubic system, and color and luster is good, the purity height, and foreign matter content is low, and is easy to operate, and equipment is simple, and hydrolysis time is short, the efficient height.
Because production of polyester is much higher than the antimonous oxide that is used for fire retardant etc. to the requirement of The catalytic antimony trioxide, its technical requirement is higher, every technical indicator of the antimonous oxide that present method is produced has has all met or exceeded the technical indicator of catalyst grade antimonous oxide, the catalytic activity of the cubic crystal antimony trioxide that the catalytic activity of product and this Jing of Ri BCR company produce is suitable, it uses add-on is 300～320ppm, the use add-on that is better than 400～500ppm of general rhomboidal crystal antimonous oxide, and the gained polyester product is all the top grade product.Therefore, the cubic crystal antimony trioxide of present method production is the good catalyst of production of polyester.
Specify method of the present invention below by embodiment.
Embodiment 1.
Get the butter of antimony solution 50ml(0.30 mole of proportion d=2.0), under agitation slowly join and contain the 9g(0.06 mole) in the solution of tartrate, 100ml ammoniacal liquor (concentration is 26-28%) and 800ml water, temperature of reaction is 25 ℃, reaction was stirred 10 minutes, the pH value of reaction back solution is 8.0, use the decantation washing precipitation,, obtain cubic crystal antimony trioxide 43g 150 ℃ of oven dry.
Embodiment 2.
Get the butter of antimony solution 50ml(0.30 mole of proportion d=2.0), under agitation slowly join and contain the 5g(0.0272 mole) in the solution of ammonium tartrate, 90ml ammoniacal liquor (concentration is 26-28%) and 500ml water, temperature of reaction is 25 ℃, reaction was stirred 10 minutes, the pH value of reaction back solution is 7.0, use the decantation washing precipitation,, obtain cubic crystal antimony trioxide 43g 110 ℃ of oven dry.
Embodiment 3.
Get the butter of antimony solution 50ml(0.30 mole of proportion d=2.0), under agitation slowly join and contain the 3g(0.0155 mole) in the solution of sodium tartrate, 120ml ammoniacal liquor (concentration is 26-28%) and 400ml water, temperature of reaction is 25 ℃, reaction was stirred 10 minutes, the pH value of reaction back solution is 10, use the decantation washing precipitation,, obtain cubic crystal antimony trioxide 43g 130 ℃ of oven dry.
Embodiment 4.
Get the butter of antimony solution 100ml(0.60 mole of proportion d=2.0), under agitation slowly join and contain the 3.5g(0.0233 mole) in the solution of tartrate, 200ml ammoniacal liquor (concentration is 26-28%) and 500ml water, temperature of reaction is 35 ℃, reaction was stirred 15 minutes, the pH value of reaction back solution is 8.0, use the decantation washing precipitation,, obtain cubic crystal antimony trioxide 86g 150 ℃ of oven dry.
Embodiment 5.
Get the butter of antimony solution 10L(60 mole of proportion d=2.0), under agitation slowly join and contain the 400g(2.66 mole) in the solution of tartrate, 20L ammoniacal liquor (concentration is 26-28%) and 50L water, the joining day of butter of antimony solution is 15 minutes, temperature of reaction is 60 ℃, reaction was stirred 30 minutes, the pH value of reaction back solution is 8.0, with drying down at 150 ℃ after the washing of precipitate, obtains cubic crystal antimony trioxide 8500g.
The smart BCR of table 1 the present invention and Ri Ben company product index relatively
| This Jing of Ri BCR company control of product standard | The embodiment of the invention 4 products obtained therefrom analytical resultss | ||
| Color and luster | -L value-a value-b value | ≥80 ≤1 ≤5 | 94 0 2 |
| Crystalline structure | 100% cubic system | 100% cubic system | |
| Purity (%) | ≥99.5 | 99.7 | |
| Ag(%) | ≤0.11 | 0.01 | |
| Pb(%) | ≤0.05 | ＜0.01 | |
| Fe(%) | ≤0.01 | ＜0.005 | |
| Vitriol (%) | ≤0.02 | ＜0.005 | |
Table 1 has been listed the data of the embodiment of the invention 4 products obtained therefrom analytical resultss and the smart BCR of Ri Ben company control of product standard, the quality product of table 1 explanation the invention process gained has met or exceeded the technical indicator of catalyst grade antimonous oxide, is the good catalyst of production of polyester.
Claims (6)
1, a kind of method for preparing cubic crystal antimony trioxide ties up in the alkaline aqueous solution butter of antimony solution direct hydrolysis, obtains cubic crystal antimony trioxide through washing and oven dry.It is characterized in that having used in the hydrolysis reaction tartrate or tartrate as coordination agent, the mol ratio of ANTIMONY TRIOXIDE SB 203 99.8 PCT and coordination agent is 1-26: 1, and hydrolysising reacting temperature is 10-80 ℃, alkaline aqueous solution adopts ammoniacal liquor or sodium carbonate solution.
2,, it is characterized in that used tartrate is sodium tartrate or ammonium tartrate according to the method for claim 1.
3, according to the method for claim 1, it is characterized in that having adopted tartrate as coordination agent, butter of antimony and tartaric mol ratio are 15-26: 1, basic solution is an ammoniacal liquor, the consumption of strong aqua is 1.5-3.5 a times of butter of antimony liquor capacity, and the consumption of water is 3-20 a times of butter of antimony liquor capacity.
4, according to the method for claim 3, it is characterized in that hydrolysis reaction carries out at ambient temperature, the pH value of reaction back solution is 7-8.
5,, it is characterized in that hydrolysis time is 10-30 minute according to the method for claim 1.
6, according to the method for claim 1, the bake out temperature that it is characterized in that product is 100-160 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92114236 CN1028290C (en) | 1992-12-12 | 1992-12-12 | Preparation method of cubic crystal antimony trioxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92114236 CN1028290C (en) | 1992-12-12 | 1992-12-12 | Preparation method of cubic crystal antimony trioxide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1072392A true CN1072392A (en) | 1993-05-26 |
| CN1028290C CN1028290C (en) | 1995-04-26 |
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ID=4946851
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92114236 Expired - Fee Related CN1028290C (en) | 1992-12-12 | 1992-12-12 | Preparation method of cubic crystal antimony trioxide |
Country Status (1)
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|---|---|
| CN (1) | CN1028290C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100344369C (en) * | 2003-11-24 | 2007-10-24 | 中国科学院大连化学物理研究所 | Antimony oxide catalyst for preparing quadri-aldehyde by selective oxidation of methane |
| CN102139919A (en) * | 2011-02-21 | 2011-08-03 | 湖南辰州矿业股份有限公司 | Method for reducing arsenic and lead in production of antimonous oxide by wet process |
| CN102259912A (en) * | 2011-06-29 | 2011-11-30 | 天津市风船化学试剂科技有限公司 | Method for preparing high-purity antimony pentasulfide |
| CN102976407A (en) * | 2012-09-19 | 2013-03-20 | 湖南辰州矿业股份有限公司 | Method for increasing diantimony trioxide particle size during wet production process of diantimony trioxide |
| CN104355332A (en) * | 2014-10-20 | 2015-02-18 | 广西高中阀门制造有限责任公司 | Preparation device of antimony trioxide for polyester |
| CN105540664A (en) * | 2016-02-22 | 2016-05-04 | 锡矿山闪星锑业有限责任公司 | Method for preparing antimony trioxide coarse in particle and high in cubic crystal form content |
| CN107629486A (en) * | 2017-11-06 | 2018-01-26 | 广西生富锑业科技股份有限公司 | A kind of preparation method of ultrawhite antimony oxide |
| CN110629042A (en) * | 2019-11-05 | 2019-12-31 | 湖南工业大学 | Method for leaching antimony oxide material by tartaric acid system and producing metallic antimony by electrodeposition |
-
1992
- 1992-12-12 CN CN 92114236 patent/CN1028290C/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100344369C (en) * | 2003-11-24 | 2007-10-24 | 中国科学院大连化学物理研究所 | Antimony oxide catalyst for preparing quadri-aldehyde by selective oxidation of methane |
| CN102139919A (en) * | 2011-02-21 | 2011-08-03 | 湖南辰州矿业股份有限公司 | Method for reducing arsenic and lead in production of antimonous oxide by wet process |
| CN102139919B (en) * | 2011-02-21 | 2012-09-05 | 湖南辰州矿业股份有限公司 | Method for reducing arsenic and lead in production of antimonous oxide by wet process |
| CN102259912A (en) * | 2011-06-29 | 2011-11-30 | 天津市风船化学试剂科技有限公司 | Method for preparing high-purity antimony pentasulfide |
| CN102259912B (en) * | 2011-06-29 | 2012-11-14 | 天津市风船化学试剂科技有限公司 | Method for preparing high-purity antimony pentasulfide |
| CN102976407B (en) * | 2012-09-19 | 2015-07-29 | 湖南辰州矿业股份有限公司 | A kind of method promoting its granularity in wet production antimonous oxide process |
| CN102976407A (en) * | 2012-09-19 | 2013-03-20 | 湖南辰州矿业股份有限公司 | Method for increasing diantimony trioxide particle size during wet production process of diantimony trioxide |
| CN104355332A (en) * | 2014-10-20 | 2015-02-18 | 广西高中阀门制造有限责任公司 | Preparation device of antimony trioxide for polyester |
| CN105540664A (en) * | 2016-02-22 | 2016-05-04 | 锡矿山闪星锑业有限责任公司 | Method for preparing antimony trioxide coarse in particle and high in cubic crystal form content |
| CN105540664B (en) * | 2016-02-22 | 2017-06-23 | 锡矿山闪星锑业有限责任公司 | A kind of preparation method of coarse granule, cubic content antimony oxide high |
| CN107629486A (en) * | 2017-11-06 | 2018-01-26 | 广西生富锑业科技股份有限公司 | A kind of preparation method of ultrawhite antimony oxide |
| CN107629486B (en) * | 2017-11-06 | 2020-05-15 | 广西生富锑业科技股份有限公司 | Preparation method of super-white antimony trioxide |
| CN110629042A (en) * | 2019-11-05 | 2019-12-31 | 湖南工业大学 | Method for leaching antimony oxide material by tartaric acid system and producing metallic antimony by electrodeposition |
| CN110629042B (en) * | 2019-11-05 | 2021-11-26 | 湖南工业大学 | Method for leaching antimony oxide material by tartaric acid system and producing metallic antimony by electrodeposition |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1028290C (en) | 1995-04-26 |
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