CN109019680A - A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method - Google Patents

A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method Download PDF

Info

Publication number
CN109019680A
CN109019680A CN201811234160.7A CN201811234160A CN109019680A CN 109019680 A CN109019680 A CN 109019680A CN 201811234160 A CN201811234160 A CN 201811234160A CN 109019680 A CN109019680 A CN 109019680A
Authority
CN
China
Prior art keywords
hydrochloric acid
titanium dioxide
titanium
tiocl
chloride
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
CN201811234160.7A
Other languages
Chinese (zh)
Inventor
唐红梅
邓科
阳丽
高凯歌
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.)
Yibin University
Original Assignee
Yibin University
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 Yibin University filed Critical Yibin University
Priority to CN201811234160.7A priority Critical patent/CN109019680A/en
Publication of CN109019680A publication Critical patent/CN109019680A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G23/00Compounds of titanium
    • C01G23/04Oxides; Hydroxides
    • C01G23/047Titanium dioxide
    • C01G23/053Producing by wet processes, e.g. hydrolysing titanium salts
    • C01G23/0536Producing by wet processes, e.g. hydrolysing titanium salts by hydrolysing chloride-containing salts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

The present invention relates to a kind of methods of titanium dioxide, specifically using containing TiOCl2Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid and ilmenite concentrate carry out acidolysis reaction, after separation removes the acid non-soluble substances such as silica therein, it is hydrolyzed acidolysis titanium liquid to obtain titanium dioxide crude product, titanium dioxide finished product is obtained after titanium dioxide crude product is washed and post-processed again, and the frerrous chloride crystal of high-quality can be then made in hydrolyzate after recrystallization.

Description

A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method
Technical field
The present invention relates to a kind of methods of titanium dioxide, belong to titanium chemical field.Specifically using containing TiOCl2's Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid and ilmenite concentrate carry out acidolysis reaction, after separation removes the acid non-soluble substances such as silica therein, Acidolysis titanium liquid is hydrolyzed to obtain titanium dioxide crude product, then obtains titanium white after titanium dioxide crude product is washed and post-processed Powder finished product.Belong to titanium chemical field.
Background technique
In the production process of Titanium Dioxide Produced by Chloride Procedure, there are two types of the tail gas acid-washing waste acids of chloride process: it is dense that one is hydrochloric acid The HCl of degree about 20%, wherein containing TiOCl2Concentration is 10.2% or so;Another kind is the HCl that concentration of hydrochloric acid is about 28%, TiOCl2Concentration is 1.2% or so.Containing TiOCl using this2When the hydrochloric acid of impurity, TiOCl2It can be with free hydrochloric acid concentration It reduces and hydrolysis occurs, TiO is precipitated2, the fine grained TiO of this hydrolysis precipitation2It is present in reaction system as solid phase impurity In, cause the application field of this hydrochloric acid to be very restricted.
There is researcher to develop a kind of method that titanium white chloride by-product hydrochloric acid is used for titanium dioxide coating, this method by pair Chlorinated exhaust washing recycling contains TiOCl2Crude salt acid as coating agent by using inorganic and organic composite coating process Coating is carried out to titanium dioxide, hydrophily, resistance to chalking, reducing power and the colour retention of titanium dioxide can be improved, but in hydrochloric acid TiOCl2It hydrolyzes not fully, and hydrochloric acid and is underutilized in the process, this process is only to use hydrochloric acid Once, titanium chlorine resource therein is not utilized effectively.
There are also researchers to disclose waste hydrochloric acid produced by chlorination elution tail gas process in a kind of production of Titanium Dioxide Produced by Chloride Procedure The acid tail gas generated in chloridising production process is directly passed through water scrubber by method of comprehensive utilization, this method, the tail after washing Gas passes through caustic wash tower again, then qualified discharge.Alkaline matter is added in the acid waste water generated into water-washing process, adjusts its pH Make the TiOCl in solution2TiO is generated in hydrolysis2Solution is then filtered by insoluble matter, and filter residue recycles.This method is logical Cross simple neutralize so that TiOCl2It is hydrolyzed to TiO2Become solid waste, solution obtains the chlorate of low value, without real Now there is the resource utilization of higher-value to it.
In addition, chlorinated exhaust pickling is contained there are also using the carbon monoxide in chlorinated exhaust as heat source TiOCl2The de- analysis of the by-product hydrochloric acid method that obtains high-purity hydrogen chloride.Although this method can obtain the de- analysis recycling of hydrochloric acid therein The hydrogen chloride of higher quality, but TiOCl therein2The TiO of precipitation is hydrolyzed during hydrochloric acid de- analysis2But at solid waste, not It is able to achieve the resource utilization to it.
There is also prepare TiO using Titanium Dioxide Produced by Chloride Procedure exhaust gas2And the method for HCl solution, this method is by chloridising titanium Chlorination exhaust gas in white powder production process is passed through pickling tower, the TiCl that will be contained in exhaust gas by spraying 18 ~ 22% dilute hydrochloric acid4It inhales It receives, TiCl in hydrochloric acid solution4It meets water and hydrolysis occurs, generate TiOCl2And HCl is given up chlorination by two-stage membrane filtration system What gas generated contains TiOCl2Hydrochloric acid solution separated, obtain hydrochloric acid solution and TiOCl2Hydrolyze the TiO generated2.This method It is filtered using film by TiOCl2It is separated with HCl, efficiency is lower to cause its econmics comparison poor.
Therefore, contain TiOCl using by-product in Titanium Dioxide Produced by Chloride Procedure production process to be efficient2Hydrochloric acid, the present invention combine The production process of hydrochloric acid method titanium dioxide allows the gold such as iron oxide therein, calcium oxide, magnesia using hydrochloric acidolysis ilmenite concentrate While belonging to oxide generation chlorate, the titanium oxide in ilmenite concentrate mutually can also be reacted with hydrochloric acid generates TiOCl2, it is incorporated in The TiOCl originally contained in this titanium chloride white powder by-product hydrochloric acid2, by hydrolyzing it as TiO2Crude product, crude product warp are located later Titanium dioxide finished product is obtained after reason.Mother liquor containing iron chloride salt and hydrochloric acid after hydrolysis then passes through evaporation and concentration and obtains frerrous chloride Saturated solution, then it is crystallized in 10 ~ 15 DEG C of mixture of ice and water below, frerrous chloride crystal is precipitated, it is made after recrystallization Obtain the frerrous chloride crystal of high-quality;Steam containing hydrogen chloride, which is condensed into after hydrochloric acid, then returns to ilmenite concentrate acidolysis system circulation benefit With.
Main chemical reactions equation in ilmenite concentrate acid hemolysis process are as follows:
FeO·TiO2+4HCl= FeCl2+ TiOCl2+2H2O
Fe2O3·TiO2+8HCl=2FeCl3+TiOCl2+4H2O
MgO·TiO2+4HCl=MgCl2+TiOCl2+2H2O
CaO·TiO2+4HCl=CaCl2+TiOCl2+2H2O
TiOCl2Hydrolysis generates TiO2Chemical equation are as follows:
TiOCl2+H2O=TiO2↓+2HCl 。
Summary of the invention
It is an object of the invention to utilize to contain TiOCl2Titanium white chloride by-product hydrochloric acid acidolysis ilmenite concentrate generation be rich in TiOCl2Acidolysis titanium liquid, and then hydrolyze and further work-up obtain titanium dioxide finished product.The present invention allows Titanium Dioxide Produced by Chloride Procedure pair Produce the TiOCl contained originally in hydrochloric acid2With the TiOCl obtained after hydrochloric acid and ilmenite concentrate acidolysis2It is integrated, and is eventually become Titanium dioxide finished product, makes the titanium elements in titanium white chloride by-product hydrochloric acid obtain high value added utilization, and chlorine element also achieves sufficiently Utilization, overcome in existing method to the disadvantage of its titanium elements and the lower deficiency of chlorine element utilization efficiency, effectively realize The high-efficiency resource recycling of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid.
The object of the present invention is achieved like this:
It measures a certain amount of containing TiOCl2Titanium white chloride by-product hydrochloric acid be added in acidolysis reaction kettle, while according to certain acid Mine handles ilmenite concentrate than the quantitative dehydration and drying that passes through is added, and closes the inlet valve of acidolysis reaction kettle.Toward the folder of acidolysis reaction kettle Be passed through steam in set to be heated, keep acidolysis temperature at 85 ~ 95 DEG C, and open stirring, make the metal oxide of ilmenite concentrate with Hydrochloric acid, which comes into full contact with, to be reacted.During acidolysis reaction, the condensation hydrochloric acid that subsequent flash distillation hydrolyzing process generates is supplemented In acidolysis reaction kettle, the acidity of reaction system is maintained.After reaction, reactant is filtered, separation insoluble solids are residual After slag, titanium liquid is obtained.
The titanium liquid for having separated acid non-soluble substance is heated to 105 ~ 115 DEG C by graphite heat exchanger, is then delivered to flash tank Carry out flash distillation hydrolysis.In this course, the TiOCl in titanium liquid2It is TiO as acid concentration reduces hydrolysis and is precipitated2Insoluble matter, can The metal chlorination salt FeCl of dissolubility2、FeCl3、MgCl2、CaCl2Deng then still remaining in solution;Then hydrolysate is divided From to TiO2Insoluble matter after washing again to its according to existing titanium dioxide postprocessing working procedures processing after obtain titanium dioxide at Product;Hydrating solution can be worth the higher frerrous chloride crystal of quality after being recrystallized.
The beneficial effects of the present invention are: containing TiOCl by utilizing2Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid to ilmenite concentrate into Row acidolysis reaction, the TiOCl generated using acidolysis reaction2And integrate original TiOCl in hydrochloric acid2It is set adequately to utilize, Soluble metal chlorination salt then passes through the frerrous chloride crystal that recrystallization is made as high-quality, and entire technical process is in raw material Titanium elements and chlorine element realize sufficient resource utilization, substantially increase the economy of the technical process.
Detailed description of the invention
Fig. 1 is the flow diagram that titanium white chloride by-product hydrochloric acid of the present invention produces titanium dioxide.
Specific embodiment
The present invention is described in further detail below with reference to embodiment, but protection scope of the present invention is not only limited in These examples.
Embodiment one: it is 7:1 according to sour mine ratio, 700g is contained to 10.2% TiOCl2Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid 100g ilmenite concentrate (the TiO of (free hydrochloric acid concentration is 21.2%) and the production of Panzhihua company246.5%、FeO2+Fe2O348.2%) It puts into acidolysis reaction kettle, it, will be subsequent during acidolysis reaction controlled at being stirred to react 3 hours under the conditions of 90 ± 2 DEG C The condensation hydrochloric acid that flash distillation hydrolysis is collected is complemented in acidolysis reaction kettle, and the free hydrochloric acid concentration of its acid hydrolysis solution is kept to be not less than 150g/L.Acidolysis mixture is filtered after acidolysis reaction, separates acid non-soluble substance therein, then acid hydrolysis solution is heated To 110 ± 2 DEG C, enters and carry out flash distillation hydrolysis in flash tank.After free acid concentration is lower than 100g/L in hydrolyzate, hydrolysis is anti- It should terminate, be filtered washing drying, obtain 80.7gTiO2Crude product, then it is post-processed obtain titanium dioxide at Product.
Embodiment two: it is 6:1 according to sour mine ratio, 600g is contained to 10.2% TiOCl2Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid 100g ilmenite concentrate (the TiO of (free hydrochloric acid concentration is 21.2%) and the production of Hainan company248.1%、FeO2+Fe2O349.3%) it throws Enter into acidolysis reaction kettle, controlled at being stirred to react 3 hours under the conditions of 90 ± 2 DEG C, by subsequent sudden strain of a muscle during acidolysis reaction It steams the condensation hydrochloric acid that hydrolysis is collected to be complemented in acidolysis reaction kettle, keeps the free hydrochloric acid concentration of its acid hydrolysis solution not less than 150g/ L.Acidolysis mixture is filtered after acidolysis reaction, acid non-soluble substance therein is separated, 110 then is heated to acid hydrolysis solution It ± 2 DEG C, enters and carries out flash distillation hydrolysis in flash tank.After free acid concentration is lower than 100g/L in hydrolyzate, hydrolysis knot Beam is filtered washing drying, obtains 78.7gTiO2Then crude product post-processes it to obtain titanium dioxide finished product.

Claims (5)

1. a kind of production method of titanium dioxide, it is characterised in that using containing TiOCl2Titanium chloride white powder by-product hydrochloric acid to titanium Concentrate carries out acidolysis reaction, and the acidolysis titanium liquid after isolating acid non-soluble substance is under conditions of free hydrochloric acid concentration is not less than 150g/L It carries out flash distillation water solution and obtains TiO2Crude product is filtered, washed, calcines and post-processes TiO2Rutile type titanium white is obtained after crude product.
2. according to the method described in claim 1, it is characterized in that being 85 ~ 95 DEG C to the acidolysis reaction temperature of ilmenite concentrate.
3. according to the method described in claim 1, it is characterized in that ilmenite concentrate carry out acidolysis reaction hydrochloric acid be containing TiOCl2Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid.
4. according to the method described in claim 1, it is characterized in that the hydrolysis of titanium liquid is carried out in the solution containing frerrous chloride 's.
5. according to the method described in claim 1, it is characterized in that it is 100 ~ 150g/ that the hydrolysis of titanium liquid, which is in free hydrochloric acid concentration, It is carried out under conditions of L.
CN201811234160.7A 2018-10-23 2018-10-23 A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method Pending CN109019680A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811234160.7A CN109019680A (en) 2018-10-23 2018-10-23 A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811234160.7A CN109019680A (en) 2018-10-23 2018-10-23 A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method

Publications (1)

Publication Number Publication Date
CN109019680A true CN109019680A (en) 2018-12-18

Family

ID=64613756

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811234160.7A Pending CN109019680A (en) 2018-10-23 2018-10-23 A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method

Country Status (1)

Country Link
CN (1) CN109019680A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115109437A (en) * 2022-07-12 2022-09-27 龙佰禄丰钛业有限公司 Preparation method of composite titanium dioxide
CN115820001A (en) * 2022-11-28 2023-03-21 攀钢集团研究院有限公司 Method for coating titanium dioxide by using hydrochloric acid as chlorination by-product
CN115974166A (en) * 2022-12-08 2023-04-18 攀枝花全瑞实业有限公司 Method for preparing high-chloride-ion pure ferrous chloride solution in industrial production of titanium dioxide by hydrochloric acid method

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2315742B (en) * 1996-07-26 2000-08-30 Tiomin Resources Inc Method for the production of synthetic rutile
CN1689975A (en) * 2004-04-27 2005-11-02 天津科技大学 Technique for producing high purity nanometer titanium dioxide
CN101723448A (en) * 2009-12-29 2010-06-09 攀钢集团研究院有限公司 Method for preparing titaniferous solution
CN102616842A (en) * 2012-04-01 2012-08-01 攀枝花新中钛科技有限公司 Method for preparing titanium white
CN102745742A (en) * 2012-07-18 2012-10-24 云南昆欧科技有限责任公司 Method for producing titanium-rich material by processing vanadium-titanium-containing blast furnace slag with titanium white waste acid
CN104192898A (en) * 2014-09-11 2014-12-10 福建坤彩材料科技有限责任公司 Preparation method for directly synthesizing titanium dioxide in titanium-rich organic phase prepared from ilmenite
CN105883917A (en) * 2016-05-26 2016-08-24 宜宾天原集团股份有限公司 Method for preparing TiO2 and HCl solution from chlorination process titanium dioxide waste gas
CN107572584A (en) * 2017-09-29 2018-01-12 福州琪宁精细化工有限公司 A kind of preparation method of titanium dioxide

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2315742B (en) * 1996-07-26 2000-08-30 Tiomin Resources Inc Method for the production of synthetic rutile
CN1689975A (en) * 2004-04-27 2005-11-02 天津科技大学 Technique for producing high purity nanometer titanium dioxide
CN101723448A (en) * 2009-12-29 2010-06-09 攀钢集团研究院有限公司 Method for preparing titaniferous solution
CN102616842A (en) * 2012-04-01 2012-08-01 攀枝花新中钛科技有限公司 Method for preparing titanium white
CN102745742A (en) * 2012-07-18 2012-10-24 云南昆欧科技有限责任公司 Method for producing titanium-rich material by processing vanadium-titanium-containing blast furnace slag with titanium white waste acid
CN104192898A (en) * 2014-09-11 2014-12-10 福建坤彩材料科技有限责任公司 Preparation method for directly synthesizing titanium dioxide in titanium-rich organic phase prepared from ilmenite
CN105883917A (en) * 2016-05-26 2016-08-24 宜宾天原集团股份有限公司 Method for preparing TiO2 and HCl solution from chlorination process titanium dioxide waste gas
CN107572584A (en) * 2017-09-29 2018-01-12 福州琪宁精细化工有限公司 A kind of preparation method of titanium dioxide

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
叶恩东: "攀枝花钛精矿制备高品质富钛料工艺分析", 《研究与开发》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115109437A (en) * 2022-07-12 2022-09-27 龙佰禄丰钛业有限公司 Preparation method of composite titanium dioxide
CN115820001A (en) * 2022-11-28 2023-03-21 攀钢集团研究院有限公司 Method for coating titanium dioxide by using hydrochloric acid as chlorination by-product
CN115974166A (en) * 2022-12-08 2023-04-18 攀枝花全瑞实业有限公司 Method for preparing high-chloride-ion pure ferrous chloride solution in industrial production of titanium dioxide by hydrochloric acid method

Similar Documents

Publication Publication Date Title
CN100357361C (en) Method for preparing high purity iron oxide yellow and iron oxide red using titanium dioxide byproduct ferrous sulfate
CN106044799B (en) Titanium chloride slag and its method for comprehensive utilization of filtrate in chloride process titanium dioxide powder craft
CN109019680A (en) A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method
CN100542968C (en) Utilize the method for sodium hydroxide clean production of titanium dioxide
CN104310467B (en) Comprehensive utilization method of high titanium slag
CN103011296B (en) Production process for high purity manganese sulfate through reduction with pyrolusite powder as raw material
CN110589884B (en) Method for recycling waste and side-product titanium oxychloride
CN109319827A (en) A kind of preparation method of germanium dioxide
CN107954474A (en) A kind of method that vanadium product and chromium sulfate basic are produced using vanadium chromium solution
CN110482592B (en) Process for preparing nano zinc oxide from steelmaking ash
CN107720801A (en) A kind of method that blanc fixe is prepared using titanium white waste acid
CN1990460B (en) Comprehensive treatment of glycine crystallization mother liquid
CN110438347A (en) Sodium cleans extraction vanadium method
CN109110807A (en) A kind of method of coproduction synthetic rutile and sulfuric acid method titanium pigment
CN107128927A (en) A kind of fine coal lime balls chlorination electrolytic preparation metallic aluminium and the method for comprehensive utilization
CN107128957B (en) A kind of fine coal lime balls chlorination electrolytic preparation aluminium oxide and the method for comprehensive utilization
CN106521555B (en) A kind of method of antimony electrolyte selectivity iron removaling
CN101462985B (en) Clean production process for azobisformamide
CN109694092A (en) A kind of comprehensive processing method of the solid waste containing chlorine
CN107188127B (en) Method for preparing titanium dioxide seed crystal by using chlorination waste acid
CN107200342A (en) A kind of flyash chlorination electrolytic preparation aluminum oxide and the method for comprehensive utilization
CN111591959A (en) Method for co-producing barium chloride and ceramic titanium white by-product hydrochloric acid of chlorination-process titanium dioxide
JP2008143763A (en) Manufacturing method of titanium dioxide, calcium sulfate and iron oxide from waste acid generated in manufacturing process of titanium dioxide
CN101172649A (en) Method for clean production of titanium dioxide by using potassium hydroxide
CN103950976A (en) Method for preparing titanium dioxide by utilizing mixed alkali of sodium hydroxide and sodium nitrate

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20181218