CN1689975A - Technique for producing high purity nanometer titanium dioxide - Google Patents
Technique for producing high purity nanometer titanium dioxide Download PDFInfo
- Publication number
- CN1689975A CN1689975A CN 200410019084 CN200410019084A CN1689975A CN 1689975 A CN1689975 A CN 1689975A CN 200410019084 CN200410019084 CN 200410019084 CN 200410019084 A CN200410019084 A CN 200410019084A CN 1689975 A CN1689975 A CN 1689975A
- Authority
- CN
- China
- Prior art keywords
- high purity
- titanium dioxide
- sodium
- titanium
- potassium
- 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.)
- Granted
Links
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
The present invention is hydrochloric acid process of producing high purity nanometer titania in chemical field. Technologically, the present invention includes the treatment of titanium containing matter first with mineralizing agent and then hydrochloric acid solution to obtain titanium oxychloride; purifying and hydrolysis at normal pressure to obtain metatitanic acid in high purity; and low temperature roasting to dewater and to obtain high purity nanometer titania. The technological process is simple, less pollutant, low in cost and high in product performance.
Description
Affiliated field
The invention belongs to chemical field and produce the technology of nano titanium oxide, especially a kind of salt acid system production high purity nanometer titania technology.
Background technology
At present, the chlorination process production titanium dioxide that du pont company adopts has history for a long time, its technology shortcoming is that facility investment is bigger, ingredient requirement is relatively harsher, and (raw material that is adopted is a rutile ore, resource is fewer, though can use artificial rutile now, in the process of productive manpower rutile, environmental pollution is more serious); Another kind method is for adopting Production By Sulfuric Acid Process titanium dioxide, though cost is lower, technical process is long, it is big to pollute, for many years this technology state that backs on one's heels.
Existing up-to-date salt acid system is produced titanium dioxide, the method of the production titanium dioxide that adopts as U.S. E Teer sodium rice Materials Co., Ltd, it is lower that its production process and chlorination process are compared temperature, equipment is simple, but its subsequent technique promptly adopts vapour phase oxidation process in preparation titanium dioxide finished product process, the spraying equipment that this vapour phase oxidation process is used is comparatively accurate expensive, also can't realize at present at home.
Current, the purposes of high purity nanometer titania is familiar with by people more and more, but many preparation technologies have relatively high expectations to material purity and price is more expensive.How utilizing feedstock production cheap and easy to get to go out more cheap high purity nanometer titania, is the problem that domestic and international manufacturer extremely pays close attention to, and also is the key issue that can this product innovation expand various fields wide popularization and application to.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art, provide that a kind of employing raw material is easy to get, environmental pollution is little, require that equipment is simple, cost is low, the simple salt acid system of technology production high purity nanometer titania technology.
The object of the present invention is achieved like this:
The processing step of salt acid system production high purity nanometer titania technology is:
(1) adopt that to contain the titaniferous materials of titanium dioxide more than 90% be raw material, will after the mixing and stirring, carry out roasting with mineralizer under 200～950 ℃ of temperature in powder mixier after this raw material pulverizing, the time is 1～8 hour, then naturally cooling;
(2) mixture behind the naturally cooling is put into washing tank and pass to tap water to washing tank and stir and make mixture be washed till neutrality, filtered by vacuum filter then, form filter cake;
(3) this filter cake is put in the drying heater under the 100 ℃ of left and right sides temperature condition filter cake dried dry powder, put into the acidolysis reaction still after this dry powder pulverized and add 30～36% technical hydrochloric acid, acidolysis is 1～5 hour under 50～100 ℃ of temperature, obtains titanium oxychloride solution;
(4) titanium oxychloride solution being put into the vacuum concentration reactor is that 0.05-0.09Mpa, temperature are to concentrate under 40～60 ℃ of conditions in vacuum tightness, obtains the titanium oxychloride concentrated solution;
(5) this titanium oxychloride concentrated solution is placed on the interior extraction agent that adopts of anticorrosion extractor and carries out extraction separation purification, obtain more purified titanium oxychloride concentrated solution;
(6) this titanium oxychloride concentrated solution is placed on slowly stirs in the hydrolytic reaction pot and heat this concentrated solution to 65～75 ℃, add the nanometer crystal seed this moment, continuing to stir and heating rapidly makes temperature reach 95～110 ℃, under this temperature, continue hydrolysis 0.5～1.5 hour, the distilled water that adds 85～95 ℃ diluted hydrolysis 15～30 minutes, obtained nano hydrated titanium dioxide;
(7). this hydrated titanium dioxide is put into slurry tank carry out sedimentation, wash, drain and dry, and this titanium dioxide dry powder is carried out roasting under 250～850 ℃ of temperature, the dry powder of formation is the high purity nanometer titania finished product.
Above-mentioned mineralizer is oxyhydroxide, sodium or the potassium of sodium or potassium or the carbonate or the supercarbonate of ammonium.Wherein the add-on of the carbonate of the oxyhydroxide of sodium or potassium, sodium or potassium or ammonium, supercarbonate is respectively: the oxyhydroxide of titaniferous materials/sodium or potassium=1/0.5 weight ratio, the carbonate of titaniferous materials/sodium or potassium or ammonium, supercarbonate=1/1～3 weight ratio;
The reactor of above-mentioned acidolysis, vacuum concentration and hydrolysis is lining fluorine reactor;
Above-mentioned titanium oxychloride solution employed extraction agent in lining fluorine vacuum concentration reactor is the mixture of tributyl phosphate or tributyl phosphate and kerosene composition;
Above-mentioned sodium rice crystal seed is the commercially available prod that contains titanium dioxide 20～40%, its addition be in the titanium oxychloride solution contained titanium dioxide amount 2～5%.
Advantage of the present invention and positively effect are:
Present patent application will be applied on the basis of " preparation method of nano titanium oxide " (application number 02159147.4) in the end of the year 2002, further (content of titanium dioxide is more than 90% to titaniferous materials, comprising various titanium ores) handle with mineralizer earlier, use dissolving with hydrochloric acid again, obtain titanium oxychloride solution, purified, hydrolysis obtains the higher metatitanic acid of purity under condition of normal pressure, through the low-temperature bake dehydration, obtain a kind of inexpensive, high purity nanometer titania then.Whole technology is fairly simple, damage ratio is less in the production process, do not need the technology that under high-temperature roasting, makes the transition, require the equipment of use fairly simple, production cost is lower, the performance of product is relatively good, is very promising method in the at present domestic and international production high purity nanometer titania technology.
It is the method for raw material with salt acid system production high purity sodium rice titanium dioxide that the present invention adopts the titanium material of titanium dioxide more than 90% that contain cheap and easy to get both at home and abroad, this product is because low price is easier to applying at numerous areas such as coating, sensitive materials, photocatalyst material, makeup, pottery, transmitter, food product pack, plastics, environmental protection.
The present invention adopts salt acid system production high purity nanometer titania, adopts to contain the higher titaniferous materials of titanium dioxide, and energy consumption is low, equipment simple production cost is low, waste is few, and hydrochloric acid can be recycled in the technology, and byproduct has only ferric oxide.Investment cost and sulfuric acid process are suitable.The insider estimates: 1910 is the sulfuric acid process epoch, and nineteen fifty is the chlorination process epoch, and 21 century is the epoch that the salt acid system is produced titanium dioxide.
Embodiment
Below by a specific embodiment, salt acid system production high purity nanometer titania processing step is narrated (to produce 100 kilograms of high purity sodium rice titanium dioxide):
(1) adopts that to contain titaniferous materials such as ilmenite concentrate or the rutile of titanium dioxide more than 90% be raw material, to in powder mixier, be placed on after the mixing and stirring and under 850 ℃ of temperature, carry out roasting in the High Temperature Furnaces Heating Apparatus with 1: 1 mixed 150 kilograms of compound of mineralizer such as yellow soda ash and sodium bicarbonate (perhaps equivalent-sodium hydroxide, potassium hydroxide and salt of wormwood, bicarbonate of ammonia etc. all can) after 150 kilograms of pulverizing of this raw material, time is 2 hours, then naturally cooling;
(2) cooled mixture is put into washing tank and pass to tap water to washing tank mixture is washed, made mixture reach neutral, filter removing the free alkali that it includes by vacuum filter then, and form filter cake;
(3) this filter cake is put in the drying heater under the 100 ℃ of left and right sides temperature condition filter cake dried dry powder, put into lining fluoric acid solution reaction kettle after this dry powder pulverized and add 600 kilograms of 36% technical hydrochloric acids, acidolysis is 3 hours under 90 ℃ of temperature, obtains 778 kilograms of titanium oxychloride solution that contain about titanium dioxide 180g/l;
(4) titanium oxychloride solution being put into lining fluorine vacuum concentration reactor is that 0.05-0.09Mpa, temperature are to concentrate under 50 ℃ of conditions in vacuum tightness, obtains 478 kilograms of titanium oxychloride concentrated solutions, and 300 kilograms the hydrochloric acid of having an appointment in the middle of this is recovered;
(5) this titanium oxychloride concentrated solution is placed on the extraction agent that adopts extraction agent tributyl phosphate or tributyl phosphate and kerosene to form in the anticorrosion extractor and carries out extraction separation purification, to obtain more purified titanium oxychloride concentrated solution;
(6) this titanium oxychloride concentrated solution is placed on slowly stirs in the lining fluorine hydrolytic reaction pot and heat this concentrated solution to 70 ℃, add the nanometer crystal seed this moment, this sodium rice seed concentration is about 30g/l, its add-on be in the above-mentioned concentrated solution titanium dioxide total amount 4%, actual this sodium rice crystal seed that adds is 18.7 liters and gets final product.Continue to stir also rapid heating and make temperature reach 100 ℃, continue hydrolysis 1 hour, the distilled water that adds 90 ℃ diluted hydrolysis 20 minutes for 200 kilograms, obtained nano hydrated titanium dioxide;
(7) this hydrated titanium dioxide is put into slurry tank and carry out sedimentation, wash, drain, and under 100 ℃, dry, obtain 123 kilograms of nano titanium oxide dry powder;
(8) this titanium dioxide dry powder is carried out roasting under 650 ℃ of temperature, obtain purity more than 99.80%, 100 kilograms of the titanium dioxide powder finished products of sodium rice particle 20～100nm.
The mineralizer that is adopted in the above-mentioned technology is oxyhydroxide, sodium or the potassium of sodium or potassium or the carbonate or the supercarbonate of ammonium, and the carbonate of the oxyhydroxide of sodium or potassium, sodium or potassium or ammonium, the add-on of supercarbonate are respectively: the oxyhydroxide of titaniferous compound/sodium or potassium=1/0.5 weight ratio, the carbonate of titaniferous compound/sodium or potassium or ammonium, supercarbonate=1/1～3 weight ratio.
Titanium oxychloride solution employed extraction agent in extractor is the extraction agent of tributyl phosphate or tributyl phosphate and kerosene composition, to obtain more purified titanium oxychloride solution.
Described sodium rice crystal seed is the commercially available prod that contains titanium dioxide 20～40%, and its addition is 2～5% of a titanium oxychloride solution total amount.
Claims (6)
1. salt acid system production high purity nanometer titania technology is characterized in that:
Its processing step is:
(1) adopt that to contain the titaniferous materials of titanium dioxide more than 90% be raw material, will after the mixing and stirring, carry out roasting with mineralizer under 200～950 ℃ of temperature in powder mixier after this raw material pulverizing, the time is 1～8 hour, then naturally cooling;
(2) mixture behind the naturally cooling is put into washing tank and pass to tap water to washing tank and stir and make mixture be washed till neutrality, filtered by vacuum filter then, form filter cake;
(3) this filter cake is put in the drying heater under the 100 ℃ of left and right sides temperature condition filter cake dried dry powder, put into the acidolysis reaction still after this dry powder pulverized and add 30～36% technical hydrochloric acid, acidolysis is 1～5 hour under 50～100 ℃ of temperature, obtains titanium oxychloride solution;
(4) titanium oxychloride solution being put into the vacuum concentration reactor is that 0.05-0.09Mpa, temperature are to concentrate under 40～60 ℃ of conditions in vacuum tightness, obtains the titanium oxychloride concentrated solution;
(5) this titanium oxychloride concentrated solution is placed on the interior extraction agent that adopts of anticorrosion extractor and carries out extraction separation purification, obtain more purified titanium oxychloride concentrated solution;
(6) this titanium oxychloride concentrated solution is placed on slowly stirs in the hydrolytic reaction pot and heat this concentrated solution to 65～75 ℃, add the nanometer crystal seed this moment, continuing to stir and heating rapidly makes temperature reach 95～110 ℃, under this temperature, continue hydrolysis 0.5～1.5 hour, the distilled water that adds 85～95 ℃ diluted hydrolysis 15～30 minutes, obtained nano hydrated titanium dioxide;
(7). this hydrated titanium dioxide is put into slurry tank carry out sedimentation, wash, drain and dry, and this titanium dioxide dry powder is carried out roasting under 250～850 ℃ of temperature, the dry powder of formation is the high purity nanometer titania finished product.
2. salt acid system production high purity nanometer titania technology according to claim 1 is characterized in that: described mineralizer is oxyhydroxide, sodium or the potassium of sodium or potassium or the carbonate or the supercarbonate of ammonium.
3. salt acid system production high purity nanometer titania technology according to claim 1 is characterized in that: the reactor of described acidolysis, vacuum concentration and hydrolysis is lining fluorine reactor;
4. salt acid system production high purity nanometer titania technology according to claim 1 is characterized in that: titanium oxychloride solution employed extraction agent in the vacuum concentration reactor is the mixture of tributyl phosphate or tributyl phosphate and kerosene composition.
5. salt acid system production high purity nanometer titania technology according to claim 1, it is characterized in that: described sodium rice crystal seed is the commercially available prod that contains titanium dioxide 20～40%, its addition be in the titanium oxychloride solution contained titanium dioxide amount 2～5%.
6. salt acid system production high purity nanometer titania technology according to claim 1 and 2, it is characterized in that: described mineralizer is that oxyhydroxide, sodium or the potassium of sodium or potassium or the carbonate of ammonium, the add-on of supercarbonate are respectively: the oxyhydroxide of titaniferous materials/sodium or potassium=1/0.5 weight ratio, the carbonate of titaniferous materials/sodium or potassium or ammonium, supercarbonate=1/1～3 weight ratio.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200410019084XA CN100408481C (en) | 2004-04-27 | 2004-04-27 | Technique for producing high purity nanometer titanium dioxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200410019084XA CN100408481C (en) | 2004-04-27 | 2004-04-27 | Technique for producing high purity nanometer titanium dioxide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1689975A true CN1689975A (en) | 2005-11-02 |
| CN100408481C CN100408481C (en) | 2008-08-06 |
Family
ID=35345785
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB200410019084XA Expired - Fee Related CN100408481C (en) | 2004-04-27 | 2004-04-27 | Technique for producing high purity nanometer titanium dioxide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100408481C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101973580A (en) * | 2010-09-10 | 2011-02-16 | 西昌新钒钛有限公司 | Method for preparing high-purity titanium pigment by using high-purity water |
| CN104743606A (en) * | 2015-03-10 | 2015-07-01 | 丹东市化学试剂厂 | Metatitanic acid purifying method |
| CN105502482A (en) * | 2014-10-15 | 2016-04-20 | 刘浩 | Preparation method of titanium dioxide |
| CN105800677A (en) * | 2016-05-18 | 2016-07-27 | 云南林缘香料有限公司 | Production method and equipment for producing metatitanic acid through titanium dioxide slurry |
| 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 |
| CN107739842A (en) * | 2017-11-29 | 2018-02-27 | 攀钢集团攀枝花钢铁研究院有限公司 | The extracting method of titanium in titaniferous metallurgical slag |
| CN109019680A (en) * | 2018-10-23 | 2018-12-18 | 宜宾学院 | A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method |
| CN111453768A (en) * | 2020-04-08 | 2020-07-28 | 福建富仕新材料有限责任公司 | Rutile metatitanic acid, titanium white and preparation method thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5030439A (en) * | 1989-10-17 | 1991-07-09 | Kerr-Mcgee Chemical Corporation | Method for producing particulate titanium oxides |
| CN1078181C (en) * | 1997-11-14 | 2002-01-23 | 中国科学院化工冶金研究所 | Process for producing nanometre-grade titanic-schorl type titanium dioxide |
-
2004
- 2004-04-27 CN CNB200410019084XA patent/CN100408481C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101973580A (en) * | 2010-09-10 | 2011-02-16 | 西昌新钒钛有限公司 | Method for preparing high-purity titanium pigment by using high-purity water |
| CN105502482A (en) * | 2014-10-15 | 2016-04-20 | 刘浩 | Preparation method of titanium dioxide |
| CN104743606A (en) * | 2015-03-10 | 2015-07-01 | 丹东市化学试剂厂 | Metatitanic acid purifying method |
| CN104743606B (en) * | 2015-03-10 | 2016-05-18 | 丹东市化学试剂厂 | Metatitanic acid purification process |
| CN105800677A (en) * | 2016-05-18 | 2016-07-27 | 云南林缘香料有限公司 | Production method and equipment for producing metatitanic acid through titanium dioxide slurry |
| 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 |
| CN107572584B (en) * | 2017-09-29 | 2019-05-10 | 福州琪宁精细化工有限公司 | A kind of preparation method of titanium dioxide |
| CN107739842A (en) * | 2017-11-29 | 2018-02-27 | 攀钢集团攀枝花钢铁研究院有限公司 | The extracting method of titanium in titaniferous metallurgical slag |
| CN109019680A (en) * | 2018-10-23 | 2018-12-18 | 宜宾学院 | A kind of Titanium Dioxide Produced by Chloride Procedure by-product hydrochloric acid production titanium dioxide method |
| CN111453768A (en) * | 2020-04-08 | 2020-07-28 | 福建富仕新材料有限责任公司 | Rutile metatitanic acid, titanium white and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100408481C (en) | 2008-08-06 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101190802B (en) | Clean method for preparing rutile-type titanium dioxide from high-titanium slag by hydrothermal method | |
| CN112978805A (en) | Comprehensive recovery method of titanium, iron and sulfate radicals in titanium white waste acid | |
| CN100408481C (en) | Technique for producing high purity nanometer titanium dioxide | |
| CN111453768A (en) | Rutile metatitanic acid, titanium white and preparation method thereof | |
| WO2019137542A1 (en) | Method for selectively leaching and upgrading high-titanium slag | |
| CN1006635B (en) | Method for preparing titanium white power using iron-smelting blast-furnace slag containing titanium | |
| CN113401938A (en) | Titanium dioxide manufacturing method and system based on sulfur-iron-titanium co-production method | |
| CN102604435A (en) | Nano transparent iron oxide yellow pigment | |
| CN115959642A (en) | Method for utilizing hydrochloric acid byproduct of titanium dioxide chloride | |
| CN1038188C (en) | Preparation method of high-purity micro-fine rutile-type titanium dioxide | |
| CN101817551A (en) | Method for preparing lithium titanate precursor from titanic iron ore | |
| Chen et al. | The productive preparation of synthetic rutile from titanium slag via an improved microwave heating and acid-alkali joint leaching approach | |
| CN1040553C (en) | Method for treating blast furnace slag by dilute hydrochloric acid | |
| CN1163415C (en) | High-purity iron oxide red producing process with iron ore powder and other iron-bearing material | |
| CN101928484A (en) | Method for preparing sulfate/titanium dioxide composite powder from titanyl sulfate | |
| CN1125778C (en) | Method for preparing metal oxide nano material | |
| CN1958462A (en) | Method for preparing potassium ferrate by using waste liquid from acid washing steel | |
| CN1940097A (en) | Extraction of chromium from mud containing chromium by sodium-salt calcination | |
| CN1034493C (en) | Method for prodn. of titanium dioxide | |
| CN113735352B (en) | Combined treatment method for hydrofluoric acid waste liquid containing nitric acid and hydrofluoric acid waste liquid containing nitric acid | |
| CN112875762B (en) | Method for preparing iron oxide red by using iron-containing pickling waste liquid | |
| CN1264754C (en) | Preparation method of nanometer rutile type titanium dioxide | |
| CN1506311A (en) | Prepn process of nano level rutile-type titania powder | |
| CN1008356B (en) | Preparation of rutile type pigment titanium white by high activity crystal | |
| CN1156429C (en) | Method for extracting citric acid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080806 Termination date: 20100427 |