CN1664173A - Process of preparing titanium sponge by fusion electrolysis of titanium dioxide - Google Patents

Process of preparing titanium sponge by fusion electrolysis of titanium dioxide Download PDF

Info

Publication number
CN1664173A
CN1664173A CN 200410101829 CN200410101829A CN1664173A CN 1664173 A CN1664173 A CN 1664173A CN 200410101829 CN200410101829 CN 200410101829 CN 200410101829 A CN200410101829 A CN 200410101829A CN 1664173 A CN1664173 A CN 1664173A
Authority
CN
China
Prior art keywords
titanium dioxide
titanium sponge
roasting
anode
cathode
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
CN 200410101829
Other languages
Chinese (zh)
Inventor
卢惠民
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.)
University of Science and Technology Beijing USTB
Original Assignee
University of Science and Technology Beijing USTB
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 University of Science and Technology Beijing USTB filed Critical University of Science and Technology Beijing USTB
Priority to CN 200410101829 priority Critical patent/CN1664173A/en
Publication of CN1664173A publication Critical patent/CN1664173A/en
Pending legal-status Critical Current

Links

Abstract

The invention relates to a method for preparing the titanium sponge through electrolyzing the titania by fused salt. The titania applied in the cathode is formed by roasting 1-3h in the carbon reducing atmosphere and 1200-1300 Deg.c. The cathode has two forms: one is plate-like titania, which is formed through roasting the shaped titania combined with PVA adhensive in high temperature and carbon reducing atmosphere; the second is titania particles, which is formed through roasting the rectangle mesh cathode made up of non-corrosive steel or metallic titanium netting in high temperature and carbon reducing atmosphere. The electrolyte is the mixing molten salt system of calcii chloridum and lithium chloride, and the anode uses carbite or inert materials. The cathode and anode are arranged vertically, and the electrode surfaces are parallel, and the electrolyser has at least one group of anode-cathode-anode electrode, and it can set many electrodes in one electrolyser. The voltage of the controlling electrolyzer is 2.8-3.2V, the electrolyzing temperature is 850-900 Deg.c. Cleaning the cathode with the dilute hydrochloric acid and drying it, and getting the titanium sponge, which contains oxygen below 600ppm and the current efficiency is between 70-80%.

Description

A kind of method of preparing titanium sponge by fusion electrolysis of titanium dioxide
Technical field
The invention belongs to the nonferrous materials field, particularly a kind of method of preparing titanium sponge by fusion electrolysis of titanium dioxide.
Background technology
The method of generally using in world's titanium sponge industrial production is a Kroll technology, and it is by magnesium reduction TiCl 4The preparation titanium sponge.This technology has not had too big change always since setting up.This technology is made up of three parts: the one, produce thick TiCl by titaniferous ore 4The 2nd, thick TiCl 4Refining; The 3rd, magnesium reduction TiCl 4Produce titanium sponge and vacuum distilling.Kroll technology is discrete, must feed to reaction in process of production, heat and discharging operation, not only energy consumption height but also cycle long, the production cost height, environmental pollution is serious.Although it is possible that Kroll technology is carried out some improvement, facts have proved that some small technical renovation can not change expensive this present situation.Therefore, the new production technique of titanium sponge cheaply of exploitation is the target that the titanium industry member is pursued to substitute Kroll technology.Direct electrolysis TiO from fused salt 2The preparation titanium sponge, its technical process is short, simple fast, cost is low, saved the chlorination in the traditional technology, make with extra care TiCl 4, complicated procedures of forming such as magnesium reduction and vacuum distilling, can reduce the cost of titanium sponge greatly.Particularly not having emitting of chlorine, avoided the generation of polluting, is a kind of novel pollution-free green metallurgical technology.Application number is that 99808568.5 patents have proposed " fused salt electrolysis of oxygen is removed in metal oxide and the sosoloid " method, has wherein mentioned and has used TiO 2Do negative electrode, direct electrolysis TiO in fused salt 2The preparation titanium sponge.Because titanium dioxide is insulating material, and is non-conductive, directly uses TiO 2Current efficiency is low, generally about 15--25%, is difficult in industrial application.
Summary of the invention
The objective of the invention is at present fused salt electrolysis TiO 2Prepare the low shortcoming of titanium sponge current efficiency, propose a kind of method of preparing titanium sponge by fusion electrolysis of titanium dioxide, this method has high current efficiency.
A kind of preparing titanium sponge by fusion electrolysis of titanium dioxide method is characterized in that titanium dioxide that this method negative electrode adopts forms at roasting 1--3h under the carbon reduction atmosphere and in 1200--1300 ℃ of scope.Negative electrode titanium dioxide is divided into tabular and two kinds of forms of particulate state, if tabular, it is tabular for the 1--2%PVA binding agent is pressed into to add weight per-cent by titanium dioxide in the making, at roasting 2--3h under the carbon reduction atmosphere and in 1200--1300 ℃ of scope; If granular, then be earlier titanium dioxide powder to be added the pelletizing that water is made diameter 1-10mm, at roasting 1--2h under the carbon reduction atmosphere and in 1200--1300 ℃ of scope; Titanium dioxide granule after the roasting packed into make in the rectangle mesh cathode mesh 100--200 order by stainless steel or ti-alloy mesh.
The ionogen that uses is calcium chloride and lithium chloride fused salt mixt system, and wherein the lithium chloride weight percent content is 5-20%.Anode uses graphite or inert material, and when with the inert material anode, electrolytic process is emitted O 2Control flume voltage is at 2.8--3.2V; Electrolysis temperature in 850--900 ℃ of scope, electrolysis time 4--5h.Electric tank cathode and anode are arranged verticals, and electrode surface is parallel to each other, and are provided with one group of electrode that--the moon--positive mode is arranged with sun in the cell body at least, also multi-group electrode can be installed with this mode in same groove, i.e. sun--the moon--sun--the moon--sun.After electrolysis is finished, take out negative electrode, use the dilute hydrochloric acid cleaning, drying, what obtain is exactly titanium sponge.The titanium sponge that makes with this method contains oxygen and is lower than 600ppm, and current efficiency is at 70--80%.Compare with traditional Kroll technology, the electrolysis production cost reduces by 40%, and the current efficiency height has been realized cleaner production.
The characteristics of the inventive method:
Because titanium dioxide is insulating material, therefore, under carbon reduction atmosphere and high-temperature roasting, make the titania molecule deoxidation become semi-conductor, improve electrochemical deoxidising efficient in the electrolytic process; Negative electrode titanium dioxide adopts granular texture, and further fast reaction speed improves deoxidation efficient.In calcium chloride electrolyte, add lithium chloride, can improve electrolytical electric conductivity.The electrode vertical parallel is arranged, and pole span is little, accelerates deoxidation speed, and favourable current efficiency improves.
Embodiment
Embodiment one, and negative electrode is made by the titanium dioxide sintered plate, and it is added by titanium dioxide, and weight per-cent is tabular for the 2%PVA binding agent is pressed into to form under carbon reduction atmosphere and at 1250 ℃ of roasting 2h; Anode is made by inert material; Use calcium chloride and lithium chloride mixed electrolyte in the electrolytic process, wherein the lithium chloride weight percent content is 5%, and electrolysis temperature is at 850 ℃.In electrolysis, bath voltage is controlled at 2.9V, the oxonium ion of on negative electrode, overflowing, and oxonium ion moves towards anode direction under electric field action.Discharge generates oxygen on anode, electrolysis 4h, and negative electrode oxygen level 600ppm becomes titanium sponge.Negative electrode and anodic arranged vertical have increased the electrolysis area, have improved single groove productivity, and current efficiency is 70%.
Embodiment two, and electric tank cathode is made by the titanium net, interior dress titanium dioxide granule, and mesh 150 orders, interior dress titanium dioxide granule, diameter 2mm, titanium dioxide granule add water polo group by titanium dioxide powder and form, under carbon reduction atmosphere and at 1200 ℃ of roasting 1h; Anode is made by graphite; Use calcium chloride and lithium chloride mixed electrolyte in the electrolytic process, wherein the lithium chloride weight percent content is 15%, and electrolysis temperature is at 870 ℃.In electrolysis, bath voltage is controlled at 3.0V, and working process is with embodiment one, and just escaping gas is a carbonic acid gas on anode, and negative electrode oxygen level 500ppm becomes titanium sponge.Open the titanium net, take out titanium sponge, current efficiency is 80%.
Embodiment three, and electric tank cathode is made by stainless (steel) wire, interior dress titanium dioxide granule, and mesh 200 orders, interior dress titanium dioxide granule, diameter 5mm, titanium dioxide granule add water polo group by titanium dioxide powder and form, under carbon reduction atmosphere and at 1300 ℃ of roasting 2h; Anode is made by graphite; Use calcium chloride and lithium chloride mixed electrolyte in the electrolytic process, wherein the lithium chloride degree is 20%, and electrolysis temperature is at 900 ℃.In electrolysis, bath voltage is controlled at 2.8V, and working process is with embodiment one, and just escaping gas is a carbonic acid gas on anode, and negative electrode oxygen level 500ppm becomes titanium sponge.Open stainless (steel) wire, take out titanium sponge, current efficiency is 80%.
Embodiment four, and electric tank cathode is made by the titanium net, interior dress titanium dioxide granule, and mesh 100 orders, interior dress titanium dioxide granule, diameter 7mm, titanium dioxide granule add water polo group by titanium dioxide powder and form, under carbon reduction atmosphere and at 1200 ℃ of roasting 2h; Anode is made by inert material, uses calcium chloride and lithium chloride mixed electrolyte in the electrolytic process, and wherein the lithium chloride weight percent content is 15%, 870 ℃ of electrolysis temperatures.In electrolysis, bath voltage is controlled at 2.8V, and working process is with embodiment one, and escaping gas is an oxygen on anode, and negative electrode 3 oxygen level 400ppm become titanium sponge.Open the titanium net, take out titanium sponge, current efficiency is 75%.
Embodiment five, and electric tank cathode is made by the titanium dioxide sintered plate, and it is added by titanium dioxide, and weight per-cent is tabular for the 1%PVA binding agent is pressed into to form under carbon reduction atmosphere and at 1200 ℃ of roasting 3h; Anode is made by graphite; Use calcium chloride electrolyte in the electrolytic process, wherein the lithium chloride weight percent content is 10%, 870 ℃ of electrolysis temperatures.In electrolysis, bath voltage is controlled at 3.1V, and working process is with embodiment one, and just escaping gas is a carbonic acid gas on anode, and negative electrode 3 oxygen level 500ppm become titanium sponge, and current efficiency is 70%.

Claims (7)

1. the method for a preparing titanium sponge by fusion electrolysis of titanium dioxide is characterized in that titanium dioxide that this method negative electrode adopts forms at roasting 1-3h under the carbon reduction atmosphere and in 1200--1300 ℃ of scope.
2. preparation titanium sponge method as claimed in claim 1, it is characterized in that the titanium dioxide that negative electrode adopts is tabular, it is tabular for the 1--2%PVA binding agent is pressed into earlier to add weight per-cent by titanium dioxide in the making, forms at roasting 2-3h under the carbon reduction atmosphere and in 1200--1300 ℃ of scope.
3. preparation titanium sponge method as claimed in claim 1 is characterized in that negative electrode titanium dioxide is granular, earlier titanium dioxide powder is added the pelletizing that water is made diameter 1-10mm, at roasting 1-2h under the carbon reduction atmosphere and in 1200--1300 ℃ of scope; Titanium dioxide granule after the roasting packed into make in the rectangle mesh cathode mesh 100--200 order by stainless steel or ti-alloy mesh.
4. as claim 1 or 2 or 3 described preparation titanium sponge methods, it is characterized in that the ionogen that this method is used is calcium chloride and lithium chloride fused salt mixt system, wherein the lithium chloride weight percent content is 5-20%.
5. preparation titanium sponge method as claimed in claim 4 is characterized in that anode electrolytic cell made by graphite or inert material, and when with the inert material anode, electrolytic process is emitted O2.
6. preparation titanium sponge method as claimed in claim 5, it is characterized in that electric tank cathode and anode are arranged verticals, at least be provided with one group of electrode that--the moon--positive mode is arranged with sun in the mutual plain cloth cell body of electrode surface, in same groove, also multi-group electrode can be installed with this mode, i.e. sun--the moon--sun--the moon--sun.
7. preparation titanium sponge method as claimed in claim 6 is characterized in that the electrolytic tank electrolysis temperature is 850--900 ℃, and bath voltage is 2.8--3.2V, and electrolysis time is 4-5h; After electrolysis is finished, take out negative electrode, use the dilute hydrochloric acid cleaning, drying, what obtain is exactly titanium sponge.
CN 200410101829 2004-12-24 2004-12-24 Process of preparing titanium sponge by fusion electrolysis of titanium dioxide Pending CN1664173A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200410101829 CN1664173A (en) 2004-12-24 2004-12-24 Process of preparing titanium sponge by fusion electrolysis of titanium dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200410101829 CN1664173A (en) 2004-12-24 2004-12-24 Process of preparing titanium sponge by fusion electrolysis of titanium dioxide

Publications (1)

Publication Number Publication Date
CN1664173A true CN1664173A (en) 2005-09-07

Family

ID=35035475

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200410101829 Pending CN1664173A (en) 2004-12-24 2004-12-24 Process of preparing titanium sponge by fusion electrolysis of titanium dioxide

Country Status (1)

Country Link
CN (1) CN1664173A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007092398A3 (en) * 2006-02-06 2008-02-28 Du Pont Method for electrolytic production of titanium and other metal powders
CN100532653C (en) * 2006-11-03 2009-08-26 西北有色金属研究院 Method for extracting titanium from electrolyzed molten salt
CN1837411B (en) * 2006-02-17 2010-09-08 武汉大学 Method for preparing refractory active metal or alloy
CN102719857A (en) * 2012-07-03 2012-10-10 北京科技大学 Method and electrolytic tank for producing metal titanium through directive electrolysis of titanium dioxide
CN103334125A (en) * 2013-06-14 2013-10-02 中国船舶重工集团公司第七二五研究所 Method for preparing sponge titanium on special resistance furnace by molten salt electrolysis method
CN107587168A (en) * 2017-10-31 2018-01-16 成都先进金属材料产业技术研究院有限公司 The method that molten-salt electrolysis prepares Titanium

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007092398A3 (en) * 2006-02-06 2008-02-28 Du Pont Method for electrolytic production of titanium and other metal powders
CN1837411B (en) * 2006-02-17 2010-09-08 武汉大学 Method for preparing refractory active metal or alloy
CN100532653C (en) * 2006-11-03 2009-08-26 西北有色金属研究院 Method for extracting titanium from electrolyzed molten salt
CN102719857A (en) * 2012-07-03 2012-10-10 北京科技大学 Method and electrolytic tank for producing metal titanium through directive electrolysis of titanium dioxide
CN102719857B (en) * 2012-07-03 2014-08-13 北京科技大学 Method and electrolytic tank for producing metal titanium through directive electrolysis of titanium dioxide
CN103334125A (en) * 2013-06-14 2013-10-02 中国船舶重工集团公司第七二五研究所 Method for preparing sponge titanium on special resistance furnace by molten salt electrolysis method
CN103334125B (en) * 2013-06-14 2015-08-12 中国船舶重工集团公司第七二五研究所 A kind of fused salt electrolysis process that adopts on special resistors stove prepares the method for titanium sponge
CN107587168A (en) * 2017-10-31 2018-01-16 成都先进金属材料产业技术研究院有限公司 The method that molten-salt electrolysis prepares Titanium

Similar Documents

Publication Publication Date Title
CN103451682B (en) A kind of method of titaniferous soluble anode electroextraction by molten salt electrolysis titanium
CA2717887C (en) Electrochemical process for the recovery of metallic iron and sulfuric acid values from iron-rich sulfate wastes, mining residues and pickling liquors
US9963796B2 (en) Method of producing titanium metal with titanium-containing material
CN1712571A (en) Pure titanium production from titanium monoxide/titanium carbide soluble solid anode electrolysis
CN101343756B (en) Method for preparing metallic titanium with high temperature fused salt electrolysis of titanium dioxide
CN107475751A (en) A kind of device and method that pure titanium is prepared by the use of liquid alloy as electrode
CN101519789A (en) Method for preparing metallic titanium by electrolyzing titanium-circulated molten salt
CN106591892B (en) Sub- titanium oxide base soluble electrode preparation method and its application in electrolytic preparation high purity titanium
CN101457372A (en) Method for directly preparing titanium and titanium alloy by titanium-containing waste residue
CN107604388A (en) Composite anode materials and preparation method thereof, positive plate and preparation method thereof
WO2019104809A1 (en) Method for directly preparing tungsten-base alloy powder by electrolyzing discarded hard alloy
WO2014205963A1 (en) Device for preparing pure titanium by molten salt electrolysis with double electrolytic baths and process therefor
CN102703929A (en) Method for preparing Ti-Fe alloy by direct reduction of ilmenite
CN105734615B (en) A kind of method that thermoelectricity reduction prepares Titanium in fluoride smelt salt
CN109112560A (en) A method of high purity tellurium is prepared using copper telluride
CN113699560B (en) Method for preparing metallic titanium by soluble anode electrolysis of fluorine-chlorine mixed molten salt system
CN1664173A (en) Process of preparing titanium sponge by fusion electrolysis of titanium dioxide
CN109811370A (en) A kind of electrolysis-titanium carbon sulphur anode-method for preparing Titanium
CN207276744U (en) Composite anode materials and positive plate
CN103233242B (en) A kind of DSA/ lead alloy combined electrode and its preparation method and application
CN103451681A (en) Method for extracting metal titanium
CN108441893A (en) A kind of molten-salt electrolysis TiO2The method for preparing Titanium
CN2778832Y (en) Fused salt electrolysis bath for preparing titanium sponge by using titanium oxide directly as raw material
CA2517379C (en) Method for copper electrowinning in hydrochloric solution
CN114262905A (en) CO capture2Molten carbonate electrolyte and use thereof

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