CN1544336A - Chemical processing method for promotion of titanium dioxide product quality - Google Patents

Chemical processing method for promotion of titanium dioxide product quality Download PDF

Info

Publication number
CN1544336A
CN1544336A CNA2003101123833A CN200310112383A CN1544336A CN 1544336 A CN1544336 A CN 1544336A CN A2003101123833 A CNA2003101123833 A CN A2003101123833A CN 200310112383 A CN200310112383 A CN 200310112383A CN 1544336 A CN1544336 A CN 1544336A
Authority
CN
China
Prior art keywords
titanium dioxide
acid solution
hydrofluoric acid
processing method
titanium
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
CNA2003101123833A
Other languages
Chinese (zh)
Inventor
夏国春
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.)
MAOMING YUEQIAO GROUP MINING CO Ltd
Original Assignee
MAOMING YUEQIAO GROUP MINING CO Ltd
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 MAOMING YUEQIAO GROUP MINING CO Ltd filed Critical MAOMING YUEQIAO GROUP MINING CO Ltd
Priority to CNA2003101123833A priority Critical patent/CN1544336A/en
Publication of CN1544336A publication Critical patent/CN1544336A/en
Pending legal-status Critical Current

Links

Landscapes

  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

A chemical processing method for improving titanium dioxide product grade, wherein hydrofluoric acid solution is utilized for conducting acid solution erosion disposing to titanium dioxide material, then purification and dehydration are carried out. By utilizing the distinguishing feature of selectivity to erosion of titanium dioxide material by the hydrofluoric acid, impurity substance can be removed and titanium dioxide product grade can be improved.

Description

A kind of chemical treatment method that improves the titanium dioxide product grade
Technical field
The present invention relates to a kind of purification processing method of titaniferous materials, particularly a kind of chemical treatment method that improves the titanium dioxide product grade.
Background technology
Usually the production process of titanium ore generally adopts ore-dressing technique methods such as fragmentation, screening, gravity treatment, magnetic separation, electric separation and flotation, but owing to be subjected to the restriction of ore quality and ore-dressing technique method, often impurity composition that can only trip is high separates, and some and titanium dioxide is chemical combination attitude impurity such as silicon oxide, calcium oxide etc. can't be removed at all, thereby cause the finished product grade of titanium dioxide to be difficult to reach the select quality requirement, a small amount of select quality cost of selecting is also very high.Therefore can't satisfy part special industry demand, as the low silicon rutile of metallurgy industry requirement, the ferrohastingsite that ceramic industry requires etc.
For improving the content of titanium dioxide, people adopt the chemical purification method, and titanium ore or the titanium ore after above-mentioned ore-dressing technique method is handled are carried out lixiviate, and as sulfuric acid process and salt acid system etc., these methods are all on the books on relevant document and patent document.Provide " a kind of manufacture method of rutile type high-purity titanium dioxide " as patent application 96117814.0, adopt special sulfuric acid process to carry out acidolysis, technologies such as leaching is reduced, and the sedimentation filtering for crystallizing is separated, the pulverizing of hydrolysed filtrate washing drying and calcining and special auxiliary agent are made.Its advantage is; Production cost is very low, and the product purity of production is very high, reach more than 99.90%; Patent application 98113128.X provides a kind of " preparation of titanic-schorl type titanium white by hydrochloric-acid process ", in the reactor of salt tolerant acid, add dilute hydrochloric acid, in the presence of the metatitanic acid hydrolysis crystal seed, add ilmenite and reductive agent simultaneously through pulverizing, holding temperature is at 108~110 ℃, in the whole process of ilmenite decomposition and metatitanic acid hydrolysis, the existence that keeps micro-reductive agent, decompose and hydrolysis end after-filtration, metatitanic acid is separated with mother liquor, and metatitanic acid is washed, and adopts the method undecomposed mineral that granularity in the metatitanic acid is big slightly of gravity concentration to separate, add HF then with the SiO#-[2 in the metatitanic acid] remove, metatitanic acid is bleached with salt and is handled then, at last 850~900 ℃ of calcinings, and the Rutile type Titanium Dioxide of the approaching or suitable inward of the whiteness of the Rutile type Titanium Dioxide of acquisition; The method that patent application 91111933.7 provides a kind of " using fluid sulphuric acid sulphating legal system to be equipped with titanium dioxide by the anatase octahedrite washed ore of upgrading ", the anatase octahedrite of crossing with chemical treatment preconcentration and purifying (this paper is called the anatase octahedrite washed ore of upgrading), by using the sulfuric acid digestion, reaction often remains on liquid suspended state, use high acid concentration, and high temperature, under the boiling condition, so that after digestion fully, by the ingot of isolating the titanium sulfate that contains vitriol in the liquid medium, the water by thereafter or the black liquor body of recirculation, it is easy to dissolving, produces so-called " black liquor body " with efficient manner, and this black liquor body produces titanium dioxide by the processing of common other step of sulphate process, the complete required sour consumption of technology is minimum, and the discharging of pollutant effluents is also minimum.Also have patent application 95191970.9 or the like, but its production technique is generally complicated, the cost height, corrodibility is strong, and the three wastes are difficult.
Summary of the invention
The objective of the invention is to overcome the shortcoming of above-mentioned prior art and a kind of chemical treatment method that improves the titanium dioxide product grade is provided, it optionally removes the impurity in the titanium dioxide material, improve the content of titanium dioxide, satisfy demand high grade product.
Purpose of the present invention can realize by following technical measures: raw material of the present invention is the titanium dioxide material, as natural rutile, white titanium ore, high titanium ore, titanium slag, artificial rutile, rich titanium material etc., through after the conventional processing, carrying out the acid solution etch again handles, it is hydrofluoric acid solution that used acid solution is handled in etch, and raw material is added in the hydrofluoric acid solution, after the etch of certain hour, effluent discharge is cleaned, dry and get again.Hydrofluoric acid has selectivity to the etch that contains the titanium dioxide material, and titanium dioxide is insoluble to hydrofluoric acid solution, ZrO substantially 2Slightly soluble, other impurity such as SiO 2, Fe 2O 3, FeO, CaO, MgO, MnO etc. then are easy to dissolving.When these impurity were optionally dissolved, grade of titanium dioxide raise immediately, also reached simultaneously and fell silicon, falls iron and fall the purpose of sulphur, phosphorus.
Concentration is all effective to the high titanium material of etch arbitrarily though described hydrofluoric acid solution can adopt.But from shortening the production cycle, reducing spent acid solution generation and the consideration of control production cost, its concentration is 5~55%, is preferably 10~30%.
The described etch time is no less than 2 hours.
The weight ratio of described titanium dioxide material and hydrofluoric acid solution is 0.5~5.5: 1, is preferably 1.2~5: 1.
Technical scheme of the present invention is reasonable in design, utilize hydrofluoric acid to the etch of titanium dioxide material characteristics selectively, removal of contamination improves the titanium dioxide product grade, thereby promotes the value of product, satisfy the needs of manufacturing enterprise to high grade product, its processing method is simple, implements easily the efficient height, cost is low, is the good method of a Nover practical.
Embodiment
Embodiment one:
Raw material is a natural rutile, falls silicon and handles:
Etch: the concentration that adding prepares in the etching tank that has agitator is 28% hydrofluoric acid solution 100 gram, cover lids immediately; Pour the high titanium material natural rutiles of 450 grams into, ore faces is covered by acid solution fully, and cover lid immediately after the stirring, left standstill effluent discharge 24 hours then.
Clean: the natural rutile flushing with clean water, the raffinate after washing can be prepared the face supernatant mother liquor of acid solution through post precipitation next time, with abundant recovery waste liquid and reduce waste liquor contamination.After cleaning twice as stated above, in the pond, ore deposit, add an amount of clear liming, fully stir with neutralization and the remaining fluorine of sedimentation.
Dry: natural rutile can directly adopt sunlight to dry or advance to cure kiln drying, removes residual moisture.Can pack after the cooling screening.
Below be to handle forward and backward parameter:
Natural rutile: TiO before handling 2: 89.8%, SiO 2: 4.7%
Handle back natural rutile: TiO 2: 93.1%, SiO 2: 1.7%
Embodiment two:
Raw material is low grade natural rutile, produces superfine natural rutile:
Its processing method is with embodiment one, and wherein natural rutile 300 restrains, and concentration is 22% hydrofluoric acid solution 100 grams, leaves standstill 24 hours.
Below be to handle forward and backward parameter:
Natural rutile: TiO before handling 2: 89.7%, S:0.020%, P:0.023%
Handle back natural rutile: TiO 2: 95.12%, S:0.008%, P:0.018%
Embodiment three:
Its processing method is with embodiment one, and raw material is a titanium slag, adds titanium slag 200 grams, and concentration is 15% hydrofluoric acid solution 100 grams, leaves standstill 24 hours.
Below be to handle forward and backward parameter:
Titanium slag: TiO before handling 2: 88.3%
Handle back titanium slag: TiO 2: 93.6%
Embodiment four:
Its processing method is with embodiment one, and raw material is white titanium ore, adds white titanium ore 450 grams, and concentration is 28% hydrofluoric acid solution 100 grams, leaves standstill 24 hours.
Below be to handle forward and backward parameter:
White titanium ore grade: TiO before handling 2: 83.4%
Handle white titanium ore grade: the TiO in back 2: 90.3%
Embodiment five:
Its processing method is with embodiment one, and raw material is an artificial rutile, adds artificial rutile 350 grams, and concentration is 22% hydrofluoric acid solution 100 grams, leaves standstill 24 hours.
Below be to handle forward and backward parameter:
Artificial rutile: TiO before handling 2: 85.3%, FeO:6.7%
Handle back titanium slag grade: TiO 2: 90.4%, FeO:2.3%
Embodiment six:
Its processing method is with embodiment one, and raw material is the artificial rutile mine tailing, adds artificial rutile mine tailing 200 grams, and concentration is 18% hydrofluoric acid solution 100 grams, leaves standstill 24 hours.
Below be to handle forward and backward parameter:
Artificial rutile mine tailing: TiO before handling 2: 74.3%, C:0.21%
Handle back artificial rutile mine tailing: TiO 2: 81.2%, C:0.053%

Claims (5)

1, a kind of chemical treatment method that improves the titanium dioxide product grade is characterized in that the titanium dioxide material is carried out the acid solution etch to be handled, and it is hydrofluoric acid solution that used acid solution is handled in etch.
2, chemical treatment method according to claim 1 is characterized in that hydrofluoric acid solution concentration is 5~55%.
3, chemical treatment method according to claim 1, the weight ratio that it is characterized in that titanium dioxide material and hydrofluoric acid solution is 0.5~5.5: 1.
4, chemical treatment method according to claim 1 and 2 is characterized in that hydrofluoric acid solution concentration is 10~30%.
5, according to claim 1 or 3 described chemical treatment methods, the weight ratio that it is characterized in that titanium dioxide material and hydrofluoric acid solution is 1.2~5: 1.
CNA2003101123833A 2003-11-27 2003-11-27 Chemical processing method for promotion of titanium dioxide product quality Pending CN1544336A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2003101123833A CN1544336A (en) 2003-11-27 2003-11-27 Chemical processing method for promotion of titanium dioxide product quality

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2003101123833A CN1544336A (en) 2003-11-27 2003-11-27 Chemical processing method for promotion of titanium dioxide product quality

Publications (1)

Publication Number Publication Date
CN1544336A true CN1544336A (en) 2004-11-10

Family

ID=34336503

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2003101123833A Pending CN1544336A (en) 2003-11-27 2003-11-27 Chemical processing method for promotion of titanium dioxide product quality

Country Status (1)

Country Link
CN (1) CN1544336A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100391851C (en) * 2006-02-14 2008-06-04 浙江大学 Method for preparing three-dimensional nanometer structure titanium dioxide
CN102701278A (en) * 2012-06-28 2012-10-03 中山大学 Method for preparing rutile type titanium dioxide nano-particles
CN103019775A (en) * 2012-11-28 2013-04-03 北京小米科技有限责任公司 Method, device and equipment for flashing for terminal equipment
CN103317250A (en) * 2013-06-08 2013-09-25 四川汉龙新材料有限公司 Method for measuring content of rutile in electrode covering
CN109402415A (en) * 2018-07-17 2019-03-01 宜宾天原集团股份有限公司 A kind of preparation of low grade natural rutile can chlorination rich-titanium material method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100391851C (en) * 2006-02-14 2008-06-04 浙江大学 Method for preparing three-dimensional nanometer structure titanium dioxide
CN102701278A (en) * 2012-06-28 2012-10-03 中山大学 Method for preparing rutile type titanium dioxide nano-particles
CN102701278B (en) * 2012-06-28 2014-12-10 中山大学 Method for preparing rutile type titanium dioxide nano-particles
CN103019775A (en) * 2012-11-28 2013-04-03 北京小米科技有限责任公司 Method, device and equipment for flashing for terminal equipment
CN103019775B (en) * 2012-11-28 2016-04-13 小米科技有限责任公司 A kind of method of terminal device brush machine, device and equipment
CN103317250A (en) * 2013-06-08 2013-09-25 四川汉龙新材料有限公司 Method for measuring content of rutile in electrode covering
CN109402415A (en) * 2018-07-17 2019-03-01 宜宾天原集团股份有限公司 A kind of preparation of low grade natural rutile can chlorination rich-titanium material method

Similar Documents

Publication Publication Date Title
US7326390B2 (en) Production of titania
JP5171631B2 (en) Beneficiation of titanium ore
CN1285743C (en) Method for recovering titanium dioxide from titanium dioxide bearing materials like steel making slags
RU2247788C1 (en) Method for preparation of scandium oxide from red mud
CN85101989A (en) Processing method with preparation of Li 2 CO 3 by treating lithium-loaded mica with K 2 SO 4
CN101157447B (en) Method for removing ferrous and other metal salt from titanium white waste acid
WO2019137543A1 (en) Method for preparing high-purity tio2 by selectively leaching from titanium concentrate with rich oxygen
EP1135537B1 (en) Treating niobium and/or tantalum containing raw materials
CN1544336A (en) Chemical processing method for promotion of titanium dioxide product quality
JPH09512056A (en) Treatment of leachate to enhance titanium-containing materials
CN1034524A (en) From synthetic rutile, extract the method for scandium oxide
US2527257A (en) Process of separating titanium from its ores
RU2483131C1 (en) Method of making scandium oxide from red slag
CN1039805C (en) Method for prepn. of electronic grade ZrO2 by Zircon
CN1163415C (en) High-purity iron oxide red producing process with iron ore powder and other iron-bearing material
CN1262678C (en) Method for removing zinc and cobalt in cobalt dregs generated in zinc hydrometallurgy by using ultrasonic separation
CZ291224B6 (en) Production process of titanium oxide
AU2010217184A1 (en) Zinc oxide purification
RU2069181C1 (en) Process for preparing scandium oxide
CN106636684A (en) Method for enriching scandium from titanium white wastewater
JPH09512057A (en) Leaching of titanium-containing materials
JPH0388718A (en) Treatment of sulfuric acid used to produce titanium oxide by sulfuric acid process
CN1120018A (en) Method of wet-extraction for arsenic
FI92578B (en) Method for producing titanium dioxide
CN111020241A (en) Method for extracting scandium oxide from zirconium oxychloride mother liquor

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication