CN1118765A - Method for producing V2O3 - Google Patents
Method for producing V2O3 Download PDFInfo
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- CN1118765A CN1118765A CN 94111901 CN94111901A CN1118765A CN 1118765 A CN1118765 A CN 1118765A CN 94111901 CN94111901 CN 94111901 CN 94111901 A CN94111901 A CN 94111901A CN 1118765 A CN1118765 A CN 1118765A
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- gas
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- vanadous oxide
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- vanadate
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Abstract
The production method involves continuous heating granular ammonium vanadate or V2O5 in a vessel and introducing industrial gas in it, the temperature in the vessel reaches 500-650 deg.C. The reduction takes place for 15-40 min. to reduce into V2O3, then cooling to 100 Deg.C and tapping. Advantage: low reduction temperature, short reduction period, low cost.
Description
The invention belongs to the oxide technique field of vanadium, particularly relate to a kind of in the industrial method of producing vanadous oxide.
Producing the method for vanadous oxide in the prior art, is raw material with Vanadium Pentoxide in FLAKES or ammonium meta-vanadate normally, and as reductive agent, decomposition-reduction forms under high temperature or High Temperature High Pressure with ammonia, hydrogen, carbon monoxide, methane or vanadium metal, calcium, magnesium, carbon etc.
Japanese Patent 86/141, the 622 disclosed technical scheme of producing vanadous oxide is: be raw material with the Vanadium Pentoxide in FLAKES, as reductive agent, the thermal decomposition and reduction process is carried out under the stainless steel tube mesohigh with ammonia.The shortcoming that this technical scheme exists is that the recovery time reaches 4 hours, makes high pressure resistant reduction vessel cost height.
Germany electrometallurgy company page has been introduced in 1985 39 volumes of " metal " magazine the 8th phase P704～707, produces the method for vanadous oxide with methane or hydrogen reducing Vanadium Pentoxide in FLAKES.The shortcoming of its method is: reduction temperature height, complex manufacturing.
Japanese patent application 88/01320228 discloses a kind of technical scheme of producing vanadous oxide: is raw material with granularity for-150 purpose ammonium meta-vanadates, is reductive agent with hydrogen, with its thermolysis and be reduced to vanadous oxide.The shortcoming of this technical scheme is: the recovery time reaches 10～20 hours.
Japanese patent application 84/61141622 discloses with the high price barium oxide under ammonia atmosphere, is pressed under 450～650 ℃ of conditions at 0.1～1.5 atmosphere, reduces 1～6 hour, produce vanadous oxide, the shortcoming of its method is: High Temperature High Pressure, long reaction time, reduction apparatus cost height.
Japanese patent application 72/7447294 discloses with ammonium meta-vanadate and has been heated in hydrogen under 200～400 ℃ of conditions, and vanadous oxide is produced in reduction in the silica tube container, and its shortcoming is a reduction apparatus manufacturing cost height.
Shanghai Tongji University page has been introduced in " Journal of Chinese Universities " 1993 the 14th volume the 3rd phase P413～414: be raw material with the ammonium meta-vanadate, by the thermolysis mode it be decomposed into vanadous oxide.Its shortcoming is: the decomposition temperature height.
" Chengdu Univ. of Science ﹠ Technology's journal " third phase P27～30 page introduction in 1984: six ammonium vanadate are in stainless steel tube, under ammonia flow, in 850 ± 50 ℃ of reduction 1～2 hour, obtain the method for vanadous oxide, the shortcoming of this method is: the reduction temperature height, the time is long, the equipment cost height.
Above-mentioned disclosed technical scheme except that said shortcoming, also has a common shortcoming to be, employed reductive agent all is purer gas, be limited to laboratory study or small-scale production and use, be difficult to satisfy big industrial needs, and original equipment is made and the production cost height.
According to investigation, the method that external indivedual enterprises are used for the industrial production vanadous oxide is: be raw material with the ammonium poly-vanadate, utilize Sweet natural gas to be reductive agent, in heat-resisting withstand voltage nickelic stainless steel vessel, obtain vanadous oxide after 950～1000 ℃ of reduction.The shortcoming of this method is: the reduction temperature height, and reduction apparatus manufacturing cost height, the Sweet natural gas consumption is big, and for the area that does not have Sweet natural gas, this method also is restricted.
The objective of the invention is: providing a kind of is raw material with ammonium vanadate or Vanadium Pentoxide in FLAKES, produces the method for vanadous oxide as reductive agent with industrial gas.This method not only can reduce reduction temperature greatly, shorten the recovery time, and production cost is low.
The production method of the said vanadous oxide of the present invention is to realize by following technical scheme:
The method of producing vanadous oxide usually is: the ammonium vanadate of certain particle size or Vanadium Pentoxide in FLAKES are added in the external-heat container continuously, feed reducing gas, the heating ammonium vanadate made its decomposition and is reduced into vanadous oxide to certain temperature zone reduction for some time.Among the present invention, the gas of feeding is industrial gas; After being heated to furnace charge in 500～650 ℃ of temperature provinces, reduced 15～40 minutes; Cool furnace is expected below 100 ℃ and is come out of the stove, and obtains vanadous oxide.
Further be: in the aforesaid method, its raw material is ammonium poly-vanadate, ammonium meta-vanadate or Vanadium Pentoxide in FLAKES.
Further be: in the aforesaid method, wherein the external-heat container is rotary kiln, shaft furnace, multiple hearth furnace or the fluidizing furnace of general steel matter.
Further be: in the aforesaid method, its reducing gas is blast furnace gas, coke-oven gas, coal gas of converter, electric furnace coal gas, producer gas or their mixed gas.
Further be: in the aforesaid method, its method of cooling is a naturally cooling or water refrigerative mode externally under the secluding air condition.
Compared with the prior art, the present invention has following tangible advantage:
1. adopt industrial gas as reductive agent, under the low-temp low-pressure condition, realized the fast restore reaction, improved production efficiency, be more suitable in industrial production in enormous quantities.
2. technology is further simplified, and the material of reduction apparatus requires low, saves energy consumption, has significantly reduced investment and production cost.
3. Lian Jia industrial gas is easy to obtain for common metallurgical works or chemical plant, and can not do any purification processes and promptly can be used as reductive agent produce vanadous oxide on industrial production.
4. vanadium recovery reaches more than 99%.
Now illustrate concrete technical solution of the present invention:
Embodiment 1:
The production method of vanadous oxide is that the ammonium vanadate of certain particle size or Vanadium Pentoxide in FLAKES are added in the external-heat container continuously, feeds industrial gas in its container.Make by outer heating that the high-temperature zone reaches 500～650 ℃ in the container, make furnace charge pass through this temperature province generation reduction reaction 15～40 minutes, make its decomposition and be reduced to vanadous oxide.Come out of the stove below the cooling furnace charge to 100 ℃.
Embodiment 2:
The vanadous oxide production method is: the industrial ammonium poly-vanadate or the Vanadium Pentoxide in FLAKES of certain particle size, join continuously in the rotary kiln that common steel tube makes by pipeline, the mode by outer heating makes furnace charge pass through 500～650 ℃ warm area in the kiln.By pipeline blast furnace gas is imported in the rotary kiln, its input direction can be identical with the furnace charge approach axis, also can be opposite, and make furnace charge and blast furnace gas this temperature province internal reaction 15～40 minutes, be reduced to vanadous oxide.Furnace charge is come out of the stove after naturally cooling to below 100 ℃ under the condition of secluding air.The grade of the finished product vanadous oxide that obtains is greater than 99%, and the rate of recovery of vanadium is greater than 99%
Embodiment 3
The production method of vanadous oxide is: the ammonium vanadate of certain particle size is added continuously in the rotary kiln of external-heat common steel tube manufacturing, the diameter of rotary kiln is 240mm, and length is 3500mm.By pipeline blast furnace gas is inputed in the rotary kiln, it is 500～650 ℃ that outer heating makes the interior high temperature section temperature of kiln.The composition of blast furnace gas is (volume): 25～26%CO; 15～16%CO
20～1.5%H
2＜0.5%O
255～56%N
2＜0.1%CH
4The input direction of coal gas is identical with the approach axis of furnace charge or opposite.Furnace charge 500～650 ℃ of high-temperature areas in stove stopped after 15 minutes, entered the cooling section of stove, came out of the stove when naturally cooling to furnace charge below 100 ℃ under the condition of secluding air.The grade of resulting vanadous oxide finished product (weight): 66.5% ∑ V; 0.41%Na
2O+K
2O;＜0.01%As; 0.13%SiO
20.13% ∑ Fe; 0.01%P; 0.009%S.The rate of recovery of vanadium＞99%
Embodiment 4:
The production method of vanadous oxide is that the Vanadium Pentoxide in FLAKES of certain particle size is input in the shaft furnace by pipeline, and reductive agent adopts coke-oven gas, and its composition is (volume): 40～62%H
27～9%CO; 2～3%CO
22～5%N
220～22%CH
4Make by outer heating that the high-temperature zone is controlled at 500～600 ℃ in the shaft furnace, furnace charge stopped 15～20 minutes in this humidity province.The vanadous oxide grade that obtains is greater than 99%, and the rate of recovery of vanadium reaches more than 99%.
Claims (5)
1. the production method of vanadous oxide is that the ammonium vanadate of certain particle size or Vanadium Pentoxide in FLAKES are joined in the external-heat container continuously; Feed reducing gas; The heating ammonium vanadate reduces for some time to the certain temperature zone; Make its decomposition and be reduced to vanadous oxide.The present invention is characterized in that: the reducing gas of feeding is an industrial gas; After being heated to furnace charge in 500～650 ℃ of temperature provinces, reduced 15～40 minutes; Cool furnace is expected below 100 ℃ and is come out of the stove.
2. as the production method of the said vanadous oxide of claim 1, it is characterized in that: ammonium vanadate wherein is industrial ammonium poly-vanadate, ammonium meta-vanadate or Vanadium Pentoxide in FLAKES.
3. as the production method of the said vanadous oxide of claim 1, it is characterized in that: wherein the external-heat container is rotary kiln, shaft furnace, multiple hearth furnace or the fluidizing furnace etc. of industrial general steel matter system.
4. as the production method of the said vanadous oxide of claim 1, it is characterized in that: industrial gas wherein is blast furnace gas, coke-oven gas, coal gas of converter, electric furnace coal gas, producer gas or their mixed gas.
5. as the production method of the said vanadous oxide of claim 1, it is characterized in that: method of cooling wherein is that naturally cooling or water externally cool off under the secluding air condition.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94111901 CN1052460C (en) | 1994-09-15 | 1994-09-15 | Method for producing V2O3 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94111901 CN1052460C (en) | 1994-09-15 | 1994-09-15 | Method for producing V2O3 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1118765A true CN1118765A (en) | 1996-03-20 |
| CN1052460C CN1052460C (en) | 2000-05-17 |
Family
ID=5035726
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 94111901 Expired - Lifetime CN1052460C (en) | 1994-09-15 | 1994-09-15 | Method for producing V2O3 |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1052460C (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100457635C (en) * | 2006-12-12 | 2009-02-04 | 攀枝花市久欣钛业有限责任公司 | Production process of vanadium sesquioxide powder |
| CN100519424C (en) * | 2006-03-03 | 2009-07-29 | 攀钢集团攀枝花钢铁研究院 | Method for producing vanadium trioxide |
| CN101817558A (en) * | 2010-04-01 | 2010-09-01 | 长沙隆泰微波热工有限公司 | Production method of vanadium trioxide |
| CN101844809A (en) * | 2010-04-28 | 2010-09-29 | 中国科学院过程工程研究所 | System and method for producing vanadium trioxide |
| CN102092787A (en) * | 2010-12-30 | 2011-06-15 | 沈阳化工大学 | Method for continuously synthesizing vanadium trioxide |
| CN102583537A (en) * | 2012-02-27 | 2012-07-18 | 南通汉瑞实业有限公司 | Production process of vanadium trioxide |
| CN103101976A (en) * | 2013-02-19 | 2013-05-15 | 中国科学院过程工程研究所 | Preparation method of vanadium trioxide powder |
| CN102092786B (en) * | 2009-12-10 | 2014-04-02 | 中国科学院过程工程研究所 | Method for cleanly preparing vanadium oxides |
| CN103922404A (en) * | 2014-04-30 | 2014-07-16 | 攀枝花学院 | Method for preparing vanadium trioxide from vanadium pentoxide |
| CN104118910A (en) * | 2014-06-24 | 2014-10-29 | 中国科学院过程工程研究所 | Method for selectively preparing vanadium oxides and recovering hydroxides through vanadate hydrogen reduction method |
| CN106629847A (en) * | 2017-01-17 | 2017-05-10 | 中南大学 | Method for preparing vanadium trioxide from sodium-vanadate salt |
| CN106745250A (en) * | 2016-11-10 | 2017-05-31 | 陕西丰源钒业科技发展有限公司 | Aoxidize the device and piece of Vanadium production method of powdery vanadic anhydride |
| CN109136555A (en) * | 2018-08-30 | 2019-01-04 | 东北大学 | Electroreduction produces the oxide precursor of V-Ti and the preparation method of flower ball-shaped ammonium poly-vanadate |
| CN113686122A (en) * | 2021-08-12 | 2021-11-23 | 湖南烁科热工智能装备有限公司 | Continuous production rotary furnace for vanadium trioxide and use method thereof |
-
1994
- 1994-09-15 CN CN 94111901 patent/CN1052460C/en not_active Expired - Lifetime
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100519424C (en) * | 2006-03-03 | 2009-07-29 | 攀钢集团攀枝花钢铁研究院 | Method for producing vanadium trioxide |
| CN100457635C (en) * | 2006-12-12 | 2009-02-04 | 攀枝花市久欣钛业有限责任公司 | Production process of vanadium sesquioxide powder |
| CN102092786B (en) * | 2009-12-10 | 2014-04-02 | 中国科学院过程工程研究所 | Method for cleanly preparing vanadium oxides |
| CN101817558A (en) * | 2010-04-01 | 2010-09-01 | 长沙隆泰微波热工有限公司 | Production method of vanadium trioxide |
| CN101844809A (en) * | 2010-04-28 | 2010-09-29 | 中国科学院过程工程研究所 | System and method for producing vanadium trioxide |
| CN101844809B (en) * | 2010-04-28 | 2014-09-17 | 深圳中科九台资源利用研究院有限公司 | System and method for producing vanadium trioxide |
| CN102092787A (en) * | 2010-12-30 | 2011-06-15 | 沈阳化工大学 | Method for continuously synthesizing vanadium trioxide |
| CN102092787B (en) * | 2010-12-30 | 2012-07-18 | 沈阳化工大学 | Method for continuously synthesizing vanadium trioxide |
| CN102583537A (en) * | 2012-02-27 | 2012-07-18 | 南通汉瑞实业有限公司 | Production process of vanadium trioxide |
| CN102583537B (en) * | 2012-02-27 | 2014-03-05 | 南通汉瑞实业有限公司 | Production process of vanadium trioxide |
| CN103101976B (en) * | 2013-02-19 | 2015-10-28 | 中国科学院过程工程研究所 | A kind of preparation method of vanadium trioxide powder |
| CN103101976A (en) * | 2013-02-19 | 2013-05-15 | 中国科学院过程工程研究所 | Preparation method of vanadium trioxide powder |
| CN103922404A (en) * | 2014-04-30 | 2014-07-16 | 攀枝花学院 | Method for preparing vanadium trioxide from vanadium pentoxide |
| CN103922404B (en) * | 2014-04-30 | 2015-09-23 | 攀枝花学院 | Vanadium Pentoxide in FLAKES prepares the method for vanadous oxide |
| CN104118910A (en) * | 2014-06-24 | 2014-10-29 | 中国科学院过程工程研究所 | Method for selectively preparing vanadium oxides and recovering hydroxides through vanadate hydrogen reduction method |
| CN106745250A (en) * | 2016-11-10 | 2017-05-31 | 陕西丰源钒业科技发展有限公司 | Aoxidize the device and piece of Vanadium production method of powdery vanadic anhydride |
| CN106745250B (en) * | 2016-11-10 | 2019-06-14 | 陕西丰源钒业科技发展有限公司 | Aoxidize the device and piece of Vanadium production method of powdery vanadic anhydride |
| CN106629847A (en) * | 2017-01-17 | 2017-05-10 | 中南大学 | Method for preparing vanadium trioxide from sodium-vanadate salt |
| CN109136555A (en) * | 2018-08-30 | 2019-01-04 | 东北大学 | Electroreduction produces the oxide precursor of V-Ti and the preparation method of flower ball-shaped ammonium poly-vanadate |
| CN113686122A (en) * | 2021-08-12 | 2021-11-23 | 湖南烁科热工智能装备有限公司 | Continuous production rotary furnace for vanadium trioxide and use method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1052460C (en) | 2000-05-17 |
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Expiration termination date: 20140915 Granted publication date: 20000517 |