CN1217298A - Preparation of titanic-schorl type titanium white by hydrochloric -acid process - Google Patents
Preparation of titanic-schorl type titanium white by hydrochloric -acid process Download PDFInfo
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- CN1217298A CN1217298A CN 98113128 CN98113128A CN1217298A CN 1217298 A CN1217298 A CN 1217298A CN 98113128 CN98113128 CN 98113128 CN 98113128 A CN98113128 A CN 98113128A CN 1217298 A CN1217298 A CN 1217298A
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- metatitanic acid
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- hydrolysis
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- ilmenite
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Abstract
The preparation method of rutile-type titanium white by using hydrochloric acid process includes the following steps: adding dilute hydrochloric acid in acid-resistant reaction still; in the presence of metatitanic acid hydrolytic seed crystal, simultaneously adding pulverized iserite and reduction agent; keeping temp. at 108-110 deg.C, and in all the processes of iserite decomposition and metatitanic acid hydrolysis, retaining the presence of micro quantity of reduction agent; after the decomposition and hydrolysis are completed, filtering and separating the metatitanic acid from mother liquor, and water-washing metatitanic acid; adopting gravity separation method to separate out the layer grain-size undecomposed mineral material from the metatitanic acid; then adding HF to remove SiO2 from metatitanic acid; bleaching metatitanic acid and making salt treatment, and calcining at 850-900 deg.C to obtain the invented product.
Description
The invention belongs to the production method of titanium dioxide
In the reactor of salt tolerant acid, add dilute hydrochloric acid, in stirring, add metatitanic acid hydrolysis crystal seed (automatic growing crystal species), at a certain temperature, add reductive agent and ilmenite simultaneously through pulverizing.Ilmenite constantly is decomposed and the continuous hydrolysis of metatitanic acid, and in whole decomposition and hydrolytic process, reductive agent constantly is consumed, and needs constantly to replenish.The existence that in entire reaction course, must keep micro-reductive agent.After ilmenite decomposition and metatitanic acid hydrolysis end, after filtration, will contain chlorination ferrous spent acid mother liquor separately.Metatitanic acid is removed remaining iron protochloride through washing.It is thick slightly to isolate granularity through gravity concentration from metatitanic acid, the undecomposed mineral that proportion is big slightly.According to SiO in the metatitanic acid
2Content add the HF of respective amount, will generate corresponding SiF
4Gas and with SiO
2Remove.Through routine bleaching with carry out salt according to different requirements and handle, produce the commodity Rutile type Titanium Dioxide through surface treatment and pulverizing more then then 850-900 ℃ of calcining.Iron protochloride spent acid mother liquor can adopt torch firing regeneration hydrochloric acid and ferric oxide, and regeneration hydrochloric acid retrieval system is decomposed ilmenite, and ferric oxide can be made the iron oxide pigment of low gear, and iron protochloride spent acid mother liquor also can be produced the raw material { 1} of red iron oxide as wet method.The surface treatment of iron protochloride spent acid mother liquor and titanium dioxide all has sophisticated technology, not at the row of the research of this paper.
Example: in the reactor of salt tolerant acid, add 19% dilute hydrochloric acid, when being raised to 100 ℃, temperature adds metatitanic acid hydrolysis crystal, add simultaneously through the ilmenite of pulverizing and the chloride soln of low price titanium, temperature maintains 108-110 ℃ always then, in the whole process of ilmenite decomposition and metatitanic acid hydrolysis, remaining at a low price, the content of titanium is that 0.3-0.5g/g decomposed in about 6 hours and hydrolysis finishes.Filtration separates metatitanic acid with iron protochloride spent acid mother liquor.Metatitanic acid is washed, and adopts the shale shaking table that the thick slightly big slightly undecomposed mineral of proportion of the granularity in the metatitanic acid are separated.After the metatitanic acid slurrying, according to SiO in the metatitanic acid
2Content adds an amount of HF with SiO
2Remove.Bleaching and salt are handled then, 850-900 ℃ of calcining about 1 hour, obtain not surface treated Rutile type Titanium Dioxide at last, and whiteness is near the Rutile type Titanium Dioxide of inward.
{ the technology CN85-105994 technical process of 1} Xie Yahan production of iron red product from iron-containing waste liquid sees that the hydrochloric acid legal system gets rutile titanium white powder craft general flow chart to reference.
Claims (3)
1: it is characterized in that salt tolerant acid has in the reactor of stirring, add dilute hydrochloric acid, in the presence of the metatitanic acid hydrolysis crystal seed, be warmed up to certain temperature, add reductive agent and ilmenite simultaneously through pulverizing.Hydrolysis simultaneously went out metatitanic acid when hydrochloric acid decomposed ilmenite.In the process of continuous decomposition of ilmenite and metatitanic acid hydrolysis, reductive agent constantly consumes the existence that must constantly replenish and keep micro-reductive agent in whole process.When ilmenite decomposes and the metatitanic acid hydrolysis finishes, after filtration metatitanic acid is separated with iron protochloride spent acid mother liquor.Metatitanic acid adopts gravity concentration that the big slightly undecomposed mineral of the thick slightly proportion of contained granularity in the metatitanic acid are separated after washing.Then will be according to SiO in the metatitanic acid
2Content add HF and remove SiO
2Then through routine bleaching with carry out salt according to different requirements and handle, 850-900 ℃ of calcining about 1 hour, obtain not surface treated Rutile type Titanium Dioxide at last, whiteness near or suitable inward Rutile type Titanium Dioxide.
2: the reductive agent of indication in the technology is characterized in that referring to the ferric iron in the solution can be reduced to ferrous material immediately, as the muriate of titanous or the vitriol of titanous etc.
3: the gravity beneficiation equipment of indication in the technology is characterized in that referring to that the mineral that the are not decomposed granularity in the metatitanic acid is thick slightly and that proportion is big slightly separate, as hydrocyclone and shale shaking table.
Priority Applications (1)
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CN98113128A CN1079374C (en) | 1998-02-24 | 1998-02-24 | Preparation of titanic-schorl type titanium white by hydrochloric -acid process |
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CN98113128A CN1079374C (en) | 1998-02-24 | 1998-02-24 | Preparation of titanic-schorl type titanium white by hydrochloric -acid process |
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CN1217298A true CN1217298A (en) | 1999-05-26 |
CN1079374C CN1079374C (en) | 2002-02-20 |
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CN98113128A Expired - Fee Related CN1079374C (en) | 1998-02-24 | 1998-02-24 | Preparation of titanic-schorl type titanium white by hydrochloric -acid process |
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Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101116785B (en) * | 2007-08-31 | 2010-12-15 | 乐昌市银星化工有限公司 | Floating ball self-sucking titanium liquid-cleaning technique |
CN101935063A (en) * | 2009-09-02 | 2011-01-05 | 沙立林 | High titanium salt acidleach is slagged tap, the preparation method of its new purposes and titanium dioxide |
CN103741263A (en) * | 2014-01-15 | 2014-04-23 | 辽宁石油化工大学 | Preparation method of high-specific-surface porous TiO2 nano-fiber |
CN105271396A (en) * | 2015-10-23 | 2016-01-27 | 云南千盛实业有限公司 | Acidolysis method of titanium dioxide by hydrochloric acid method |
CN108002434A (en) * | 2017-11-30 | 2018-05-08 | 广西雅照钛白有限公司 | A kind of method that titanium dioxide is prepared with sulfuric acid |
CN108149015A (en) * | 2018-01-15 | 2018-06-12 | 东北大学 | A kind of method of valuable constituent element in oxygen-enriched Selectively leaching extraction vanadium titano-magnetite |
CN108217722A (en) * | 2018-03-02 | 2018-06-29 | 茂名粤桥集团矿业有限公司 | A kind of raising Reductive leaching synthetic rutile TiO2The process of grade |
CN108300875A (en) * | 2018-01-15 | 2018-07-20 | 东北大学 | A kind of oxygen-enriched Selectively leaching ilmenite concentrate prepares high purity Ti O2Method |
CN108300874A (en) * | 2018-01-15 | 2018-07-20 | 东北大学 | A kind of method of high titanium slag Selectively leaching upgrading |
CN108316926A (en) * | 2017-12-29 | 2018-07-24 | 四川江铜稀土有限责任公司 | A kind of method of differentiation explosion hydraulic mining fine-structure mesh arteries and veins REE mineralization rock |
CN109467123A (en) * | 2018-11-23 | 2019-03-15 | 宜宾天原集团股份有限公司 | A kind of artificial rutile mether liquor comprehensive resource utilizes method |
US10377639B2 (en) | 2014-09-11 | 2019-08-13 | Fujian Kuncai Material Technology Co., Ltd. | Preparation method for directly synthesizing titanium dioxide from titanium-rich organic phase prepared from ilmenite |
CN113371750A (en) * | 2021-06-08 | 2021-09-10 | 龙蟒佰利联集团股份有限公司 | Method for preparing barium sulfate by combining titanium white waste acid obtained by chlorination process and titanium white waste acid obtained by sulfuric acid process |
CN115974144A (en) * | 2021-11-27 | 2023-04-18 | 四川省有色矿冶科技有限公司 | Production process for preparing titanium dioxide by hydrochloric acid method |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
HU193372B (en) * | 1985-05-21 | 1987-09-28 | Biogal Gyogyszergyar | Process for the purification of a dextrane bead polymer of stereoscopic mesh structure suitable for pharmaceutical purposes |
CN1038188C (en) * | 1994-07-09 | 1998-04-29 | 山东大学 | Preparation method of high-purity micro-fine rutile-type titanium dioxide |
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1998
- 1998-02-24 CN CN98113128A patent/CN1079374C/en not_active Expired - Fee Related
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101116785B (en) * | 2007-08-31 | 2010-12-15 | 乐昌市银星化工有限公司 | Floating ball self-sucking titanium liquid-cleaning technique |
CN101935063A (en) * | 2009-09-02 | 2011-01-05 | 沙立林 | High titanium salt acidleach is slagged tap, the preparation method of its new purposes and titanium dioxide |
CN103741263A (en) * | 2014-01-15 | 2014-04-23 | 辽宁石油化工大学 | Preparation method of high-specific-surface porous TiO2 nano-fiber |
US10377639B2 (en) | 2014-09-11 | 2019-08-13 | Fujian Kuncai Material Technology Co., Ltd. | Preparation method for directly synthesizing titanium dioxide from titanium-rich organic phase prepared from ilmenite |
CN105271396A (en) * | 2015-10-23 | 2016-01-27 | 云南千盛实业有限公司 | Acidolysis method of titanium dioxide by hydrochloric acid method |
CN108002434A (en) * | 2017-11-30 | 2018-05-08 | 广西雅照钛白有限公司 | A kind of method that titanium dioxide is prepared with sulfuric acid |
CN108316926A (en) * | 2017-12-29 | 2018-07-24 | 四川江铜稀土有限责任公司 | A kind of method of differentiation explosion hydraulic mining fine-structure mesh arteries and veins REE mineralization rock |
CN108316926B (en) * | 2017-12-29 | 2019-06-04 | 四川江铜稀土有限责任公司 | A kind of method of differentiation explosion hydraulic mining fine-structure mesh arteries and veins REE mineralization rock |
CN108300875A (en) * | 2018-01-15 | 2018-07-20 | 东北大学 | A kind of oxygen-enriched Selectively leaching ilmenite concentrate prepares high purity Ti O2Method |
CN108300874A (en) * | 2018-01-15 | 2018-07-20 | 东北大学 | A kind of method of high titanium slag Selectively leaching upgrading |
CN108149015A (en) * | 2018-01-15 | 2018-06-12 | 东北大学 | A kind of method of valuable constituent element in oxygen-enriched Selectively leaching extraction vanadium titano-magnetite |
CN108217722A (en) * | 2018-03-02 | 2018-06-29 | 茂名粤桥集团矿业有限公司 | A kind of raising Reductive leaching synthetic rutile TiO2The process of grade |
CN109467123A (en) * | 2018-11-23 | 2019-03-15 | 宜宾天原集团股份有限公司 | A kind of artificial rutile mether liquor comprehensive resource utilizes method |
CN113371750A (en) * | 2021-06-08 | 2021-09-10 | 龙蟒佰利联集团股份有限公司 | Method for preparing barium sulfate by combining titanium white waste acid obtained by chlorination process and titanium white waste acid obtained by sulfuric acid process |
CN115974144A (en) * | 2021-11-27 | 2023-04-18 | 四川省有色矿冶科技有限公司 | Production process for preparing titanium dioxide by hydrochloric acid method |
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