CN104018010B - Reduction and distillation furnace in titanium sponge production - Google Patents
Reduction and distillation furnace in titanium sponge production Download PDFInfo
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- CN104018010B CN104018010B CN201310699573.3A CN201310699573A CN104018010B CN 104018010 B CN104018010 B CN 104018010B CN 201310699573 A CN201310699573 A CN 201310699573A CN 104018010 B CN104018010 B CN 104018010B
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Abstract
The invention discloses a kind of reduction and distillation furnace of titanium sponge production, furnace shell respectively with flange, furnace bottom connects, heating unit is provided with in furnace shell, external insulation layer, described reduction and distillation furnace is divided into the first half and Lower Half by division board, condenser is provided with in the external insulation layer of the reduction and distillation furnace first half, heat-eliminating medium inlet pipe is located at the top of division board, heat-eliminating medium goes out pipe through flange, gap and row's fistulae is provided with between base insulating layer and condenser, the upper flange in gap is provided with pressure relief opening, moderate soak layer is provided with between external insulation layer in reduction and distillation furnace bottom and base insulating layer, heat exchanger is provided with outside moderate soak layer, heat inlet pipe is arranged on the top of furnace bottom, heat goes out pipe and is arranged on below division board, the present invention can improve reduction feed rate, shorten the production cycle, improve reduction and distillation furnace bottom heat-retaining condition, power consumption and production cost can be reduced.
Description
Technical field
The invention belongs to technical field of production of sponge titanium, the reduction and distillation furnace particularly in a kind of titanium sponge production.
Background technology
Industrial production titanium sponge all adopts magnesium reduction titanium tetrachloride method both at home and abroad at present, and in reduction distillation operation, type of furnace majority adopts inverse u shape integrated process to produce, and be characterized in that single furnace output is large, qualification rate is high, the advantage that energy consumption is low.For reduce production cost, each state all using equipment enlarging as technological development direction.The reaction of magnesium reduction titanium tetrachloride is a thermopositive reaction, on reduction and distillation furnace top and reactor top, a large amount of waste heats to be produced in reduction production process, wherein react the reaction energy of a part of heat for self of generation, other heat must constantly be got rid of, otherwise temperature raises and makes reactor wall overtemperature and make shorten the work-ing life of reactor apparatus, also increase iron in reactor to velocity of diffusion in liquid magnesium, product iron content is increased, and feed time is increased, extend the titanium sponge production cycle.In reduction and distillation furnace, bottom and reactor lower part, need external heat to maintain melt temperature to ensure temperature and the magnesium chloride exhaust temperature of liquid magnesium, namely in inverse u shape produce titanium sponge by combination method, reduction phase need dispel the heat to reduction and distillation furnace top, need be incubated whole reduction distillation when distilling, in existing reduction and distillation furnace, between reduction period, top heat generally adopts external ventilation to distribute, unrealized recycling.
Summary of the invention
Have problems for solving in prior art, the invention provides the reduction and distillation furnace in a kind of titanium sponge production, adjustable upper and lower two temperature at different times of reduction and distillation furnace in process of production, the a large amount of residual heat of reaction in reactor top can be discharged in time when reducing, increase feed rate, shorten the production cycle, and utilize the heat energy that recoverable reduction is discharged in time, supply reduction and distillation furnace bottom and distillation use, and reduce production energy consumption.
Technical scheme of the present invention is as described below:
Reduction and distillation furnace in titanium sponge production, primarily of furnace shell, heating unit, flange, furnace bottom forms, furnace shell respectively with flange, furnace bottom connects, heating unit is provided with in furnace shell, external insulation layer, described reduction and distillation furnace is divided into the first half and Lower Half by division board, condenser is provided with in the external insulation layer of the reduction and distillation furnace first half, heat-eliminating medium inlet pipe is located at the top of division board, heat-eliminating medium goes out pipe through flange, gap and row's fistulae is provided with between base insulating layer and condenser, the upper flange in gap is provided with pressure relief opening, moderate soak layer is provided with between external insulation layer in reduction and distillation furnace bottom and base insulating layer, heat exchanger is provided with outside moderate soak layer, heat inlet pipe is arranged on the top of furnace bottom, heat goes out pipe and is arranged on below division board.
Described heat-eliminating medium is gone out pipe and is connected with heat inlet pipe by pipeline.
Described condenser is tubular(surface)condenser.
Described heat exchanger is tubular heater exchhanger.
In the present invention, condenser is utilized to carry out forced heat radiation to reduction and distillation furnace top between reduction period, and heat is transported to reduction and distillation furnace by heat exchanger recycles, namely achieve the forced heat radiation effect of reduction and distillation furnace top, bottom between reduction period and have insulation effect, reach the object increasing feed rate, reduce power consumption.
Advantage of the present invention and beneficial effect:
Instant invention overcomes the problem of the feed time length that reduction and distillation furnace top heat radiation when titanium sponge production reduces causes not in time, reduction feed rate can be improved, shorten the production cycle, simultaneously, improve reduction and distillation furnace bottom heat-retaining condition, improve the effect of full stove insulation during distillation, power consumption and production cost can be reduced.
Accompanying drawing explanation
Fig. 1 is the reduction and distillation furnace schematic diagram in titanium sponge production of the present invention;
In figure: 1-heat goes out pipe, 2-arranges fistulae, 3-heat-eliminating medium goes out pipe, 4-heating unit, 5-base insulating layer, 6-pressure relief opening, 7-flange, 8-external insulation layer, 9-heat-eliminating medium inlet pipe, 10-division board, 11-moderate soak layer, 12-heat inlet pipe, 13-furnace bottom, 14-gap, 15-furnace shell.
Embodiment
Below in conjunction with accompanying drawing, the present invention is described in further detail, but should not be interpreted as that the scope of theme of the present invention is only limitted to following embodiment at this point, without departing from the idea case in the present invention described above, all make according to ordinary skill knowledge and customary means various amendments, replacement and change, include within the scope of the invention.
Embodiment one
As Fig. 1, shown in, a kind of reduction and distillation furnace of titanium sponge production, primarily of furnace shell 15, heating unit 4, flange 7, furnace bottom 13 forms, furnace shell 15 respectively with flange 7, furnace bottom 13 connects, heating unit 4 is provided with in furnace shell 15, external insulation layer 8, described reduction and distillation furnace is divided into the first half and Lower Half by division board 10, condenser is provided with in the external insulation layer 8 of the reduction and distillation furnace first half, heat-eliminating medium inlet pipe 9 is located at the top of division board 10, heat-eliminating medium goes out pipe 3 through flange 7, be provided with gap 14 between base insulating layer 5 and condenser and arrange fistulae 2, the upper flange 7 in gap 14 is provided with pressure relief opening 6, moderate soak layer 11 is provided with between external insulation layer 8 in reduction and distillation furnace bottom and base insulating layer 5, heat exchanger is provided with outside moderate soak layer 11, heat inlet pipe 12 is arranged on the top of furnace bottom 13, heat goes out pipe 1 and is arranged on below division board 10.
Further, described heat-eliminating medium is gone out pipe 3 and is connected with heat inlet pipe 12 by pipeline.
Further, described condenser is tubular(surface)condenser.
Further, described heat exchanger is tubular heater exchhanger.
Claims (4)
1. the reduction and distillation furnace in a titanium sponge production, primarily of furnace shell (15), heating unit (4), flange (7), furnace bottom (13) forms, furnace shell (15) respectively with flange (7), furnace bottom (13) connects, heating unit (4) is provided with in furnace shell (15), external insulation layer (8), it is characterized in that described reduction and distillation furnace is divided into the first half and Lower Half by division board (10), condenser is provided with in the external insulation layer (8) of the reduction and distillation furnace first half, heat-eliminating medium inlet pipe (9) is located at the top of division board (10), heat-eliminating medium goes out pipe (3) through flange (7), be provided with gap (14) between base insulating layer (5) and condenser and arrange fistulae (2), the upper flange (7) of gap (14) is provided with pressure relief opening (6), moderate soak layer (11) is provided with between external insulation layer (8) in reduction and distillation furnace bottom and base insulating layer (5), moderate soak layer is provided with heat exchanger outside (11), heat inlet pipe (12) is arranged on the top of furnace bottom (13), heat goes out pipe (1) and is arranged on division board (10) below.
2. reduction and distillation furnace according to claim 1, is characterized in that described heat-eliminating medium is gone out pipe (3) and is connected with heat inlet pipe (12) by pipeline.
3. reduction and distillation furnace according to claim 1, is characterized in that described condenser is tubular(surface)condenser.
4. reduction and distillation furnace according to claim 1, is characterized in that described heat exchanger is tubular heater exchhanger.
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CN201310699573.3A CN104018010B (en) | 2013-12-18 | 2013-12-18 | Reduction and distillation furnace in titanium sponge production |
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CN201310699573.3A CN104018010B (en) | 2013-12-18 | 2013-12-18 | Reduction and distillation furnace in titanium sponge production |
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CN104018010A CN104018010A (en) | 2014-09-03 |
CN104018010B true CN104018010B (en) | 2015-09-16 |
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Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106591602A (en) * | 2017-01-19 | 2017-04-26 | 贵州大学 | Forced convection magnesium heating method sponge titanium production reduction system and forced convection method |
CN108754184A (en) * | 2018-08-29 | 2018-11-06 | 遵义钛业股份有限公司 | A kind of reduction and distillation furnace of magnesium processes production titanium sponge |
CN110714129A (en) * | 2019-12-04 | 2020-01-21 | 遵义钛业股份有限公司 | Reduction distillation furnace used in titanium sponge reduction production |
CN111020229B (en) * | 2019-12-24 | 2022-03-29 | 新疆湘晟新材料科技有限公司 | Energy-saving durable efficient reduction distillation integrated electric furnace for producing titanium sponge |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1851015A (en) * | 2006-05-31 | 2006-10-25 | 刘晓岚 | Apparatus for making sponge iron by direct-cooled combination method |
CN200961145Y (en) * | 2006-08-01 | 2007-10-17 | 遵义钛业股份有限公司 | Combination furnace distillation channel vertical pipe sealing device |
CN101435026A (en) * | 2008-12-08 | 2009-05-20 | 洛阳双瑞万基钛业有限公司 | Titanium sponge 10-ton reduction-distillation furnace |
CN201245697Y (en) * | 2008-08-29 | 2009-05-27 | 宝钛华神钛业有限公司 | Cooling water jacket for distilling zirconium sponge |
CN201476539U (en) * | 2008-09-25 | 2010-05-19 | 贵阳铝镁设计研究院 | Forced cooling type reduction distillation furnace |
CN101724754A (en) * | 2008-10-30 | 2010-06-09 | 贵阳铝镁设计研究院 | Reduction and distillation furnace |
CN102230092A (en) * | 2011-06-24 | 2011-11-02 | 遵义钛业股份有限公司 | Reduction distillation device for producing sponge titanium by magnesium reduction process |
CN102732738A (en) * | 2012-06-15 | 2012-10-17 | 金川集团有限公司 | Reaction cylindrical shell for large reduction distilling furnace |
CN202658214U (en) * | 2012-06-15 | 2013-01-09 | 金川集团有限公司 | Reaction cylinder for large reduction distillation furnace |
CN102978420A (en) * | 2012-12-25 | 2013-03-20 | 遵义钛业股份有限公司 | Reducing device for producing titanium sponge |
CN203700458U (en) * | 2013-12-18 | 2014-07-09 | 遵义钛业股份有限公司 | Reduction distilling furnace for producing titanium sponge by virtue of magnesium reduction method |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102534262A (en) * | 2012-01-18 | 2012-07-04 | 深圳市新星轻合金材料股份有限公司 | Distillation equipment for producing titanium sponge |
-
2013
- 2013-12-18 CN CN201310699573.3A patent/CN104018010B/en active Active
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1851015A (en) * | 2006-05-31 | 2006-10-25 | 刘晓岚 | Apparatus for making sponge iron by direct-cooled combination method |
CN200961145Y (en) * | 2006-08-01 | 2007-10-17 | 遵义钛业股份有限公司 | Combination furnace distillation channel vertical pipe sealing device |
CN201245697Y (en) * | 2008-08-29 | 2009-05-27 | 宝钛华神钛业有限公司 | Cooling water jacket for distilling zirconium sponge |
CN201476539U (en) * | 2008-09-25 | 2010-05-19 | 贵阳铝镁设计研究院 | Forced cooling type reduction distillation furnace |
CN101724754A (en) * | 2008-10-30 | 2010-06-09 | 贵阳铝镁设计研究院 | Reduction and distillation furnace |
CN101435026A (en) * | 2008-12-08 | 2009-05-20 | 洛阳双瑞万基钛业有限公司 | Titanium sponge 10-ton reduction-distillation furnace |
CN102230092A (en) * | 2011-06-24 | 2011-11-02 | 遵义钛业股份有限公司 | Reduction distillation device for producing sponge titanium by magnesium reduction process |
CN102732738A (en) * | 2012-06-15 | 2012-10-17 | 金川集团有限公司 | Reaction cylindrical shell for large reduction distilling furnace |
CN202658214U (en) * | 2012-06-15 | 2013-01-09 | 金川集团有限公司 | Reaction cylinder for large reduction distillation furnace |
CN102978420A (en) * | 2012-12-25 | 2013-03-20 | 遵义钛业股份有限公司 | Reducing device for producing titanium sponge |
CN203700458U (en) * | 2013-12-18 | 2014-07-09 | 遵义钛业股份有限公司 | Reduction distilling furnace for producing titanium sponge by virtue of magnesium reduction method |
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