CN104776722A - Variable-frequency ventilation cooling system for titanium sponge and zirconium sponge - Google Patents
Variable-frequency ventilation cooling system for titanium sponge and zirconium sponge Download PDFInfo
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- CN104776722A CN104776722A CN201510123210.4A CN201510123210A CN104776722A CN 104776722 A CN104776722 A CN 104776722A CN 201510123210 A CN201510123210 A CN 201510123210A CN 104776722 A CN104776722 A CN 104776722A
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Abstract
The invention discloses a variable-frequency ventilation cooling system for titanium sponge and zirconium sponge. The variable-frequency ventilation cooling system comprises a furnace body, wherein a forced ventilation system is arranged at the upper end of the furnace body and comprises a variable-frequency fan, blast pipes and at least two annular wind collecting belts, the annular wind collecting belts are arranged up and down in parallel and are respectively arranged in the interiors of the side walls of the furnace body, the outer side of each annular wind collecting belt is connected with the variable-frequency fan respectively by virtue of the blast pipes, air inlets are uniformly formed in the inner side of each annular wind collecting belt, an exhaust annular wind collecting belt for exhausting air is arranged below the bottom annular wind collecting belt, a wind collecting pipeline is connected with the outer side of the exhaust annular wind collecting belt, and air outlets are uniformly formed in the inner side of the exhaust annular wind collecting belt. According to the variable-frequency ventilation cooling system for the titanium sponge and the zirconium sponge, the annular wind collecting belts and the exhaust annular wind collecting belt are arranged, so that air feeding and air discharging are very smooth under the power of the variable-frequency fan.
Description
Technical field
The present invention relates to titanium sponge, sponge zirconium production technical field, particularly a kind of titanium sponge, sponge zirconium variable-frequency ventilation cooling system.
Background technology
At present, sponge titanium smelting all adopts Kroll process to produce product.Mainly adopt fused salt chlorimation, I type also steam stove technology, fluidizing chlorination and the type of falling U also steam stove technology production titanium sponge abroad, domestic, mainly adopt upper magnesium chloride formula I type of arranging to go back steam stove technology with U is small-sized.Along with China's titanium sponge production technology development, production technology constantly perfect, also increasingly maximize for improving the cost-saving smelting furnace of production capacity, single furnace output improves constantly.Along with the lasting doldrums of international economy form since 2009, drop in price one tunnel of titanium sponge.How shortening single stove production cycle reduces costs and improves titanium sponge grade, has become each titanium sponge factory urgent problem.
The magnesiothermic reduction of TiCL4 is a strong exothermic reaction.Pass through actual measurement, at reduction production period, reactor central temperature is the highest exceeds 1400 DEG C, if fail in time the waste heat that reduction reaction produces to be drained, the interior external quality of titanium sponge will be affected, reduce reinforced and reaction rate, prolongation titanium sponge production cycle and increase production cost.At reduction production period, usual reactor is mainly through heat radiations such as inlet and outlet, great Gai, cooling water, furnace shell and furnace bottoms.Wherein most importantly by inlet and outlet reactor reactant liquor worn and dispel the heat.Radiating mode is got involved without external force, and reactor heat is got rid of in gravity-flow ventilation.The mode of opening airduct needs workman to climb up furnace shell outer platform, and turning on flange holding screw unloads blind plate by hand.
The shortcoming of this radiating mode mode is as follows:
1, the slow charging rate of radiating rate is low: the reduction process of TiCl4 is carried out in the solid, liquid, gas state multiphase coexistence system containing Ti, TiCl2, TiCl3, TiCl4, Mg, MgCl2, also be an exothermic reaction simultaneously, in order to maintain normal temperature, prevent the generation of ferro-titanium, good heat radiation must be carried out, and this mode just limits reduction reaction rate, charging rate (the fast 280-320kg/h of the average material) reduction cycle reducing Ticl4 is long, production cost remains high, and also constrains the maximization of equipment simultaneously.
2, reactant liquor wears the bad control of temperature: easily cause overtemperature or local overheating in production process, and it is high that temperature reaches ferrotianium lowest total of the melting point generation ferro-titanium titanium sponge iron-holder more than 1085 ° of C, and product grade declines and causes economic loss.
3, labour intensity is large exists potential safety hazard: in production process, workman will climb up the manual blind plate opening or closing all in/out air tubes of furnace wall outer platform of 3-4 rice, whole operating process needs 1-1.5 hour, work under bad environment, the narrow and small environment temperature of workbench operations area can reach 60 DEG C, easily the accident such as heatstroke and burn occurs.
Summary of the invention
The object of the invention is to make upper-lower section operating temperature in reacting furnace control in required temperature, can realize cooling faster.
For achieving the above object, the invention provides a kind of titanium sponge, sponge zirconium variable-frequency ventilation cooling system, comprise body of heater, the upper end of described body of heater is provided with forced ventilation system, described forced ventilation system comprises frequency conversion fan, blast pipe, annular collection wind band, described annular collection wind band be arranged two at least up and down in parallel, be separately positioned on the interior of body of heater, frequency conversion fan is connected to respectively by blast pipe outside each described annular collection wind band, evenly air inlet is provided with inside each described annular collection wind band, the annular of the air draft for an air draft collection wind band is also provided with below an annular collection wind band of bottom, duct set road is connected with outside described air draft annular collection wind band, evenly exhaust outlet is provided with inside described air draft annular collection wind band.Titanium sponge of the present invention, sponge zirconium variable-frequency ventilation cooling system, arrange annular collection wind band and air draft annular collection wind band, make air intake and air-out very smooth and easy under the power of frequency conversion fan.
As a further improvement on the present invention, each described air inlet is all provided with air intake arm, each described exhaust outlet is all provided with air exhaust branch pipe, in described duct set road, arranged outside has heat-insulation layer, and described duct set road is provided with electrically operated valve.Air intake arm and air exhaust branch pipe have the effect of reinforcing and leading.
As a further improvement on the present invention, blast pipe described in every root is also provided with valve, described valve is electric butterfly valve, and described electric butterfly valve and frequency conversion fan are controlled by central control system.Electric butterfly valve and frequency conversion fan are controlled by central control system, make the control accuracy of temperature higher.
As a further improvement on the present invention, at least one circle stopper is also provided with at the lower semisection of described furnace body inside wall.
Titanium sponge of the present invention, sponge zirconium variable-frequency ventilation cooling system, forced ventilation system solves 1, the slow charging rate of radiating rate is low, and radiating rate significantly improves, and TiCl4 charging rate strengthens.The original charging rate of TiCl440 ton need be added for the whole reduction process of 10t/ stove 10t stove to need to add material in 133 hours for 300kg/h, now only need 66 hours for 600kg/h feed time.2, reactant liquor surface temperature can be controlled in ± 5 DEG C meet manufacturing technique requirent completely.3, whole ventilation process achieves automation without the need to manual operation, reduces labor strength and eliminates potential safety hazard.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is the A direction view of Fig. 1;
Wherein, 1-body of heater, 2-frequency conversion fan, 3-blast pipe, 4-annular collection wind band, 5-air inlet, 6-air draft annular collection wind band, 7-duct set road, 8-exhaust outlet, 9-air intake arm, 10-air exhaust branch pipe, 11-heat-insulation layer, 12-electrically operated valve, 13-electric butterfly valve, 14-central control system, 15-stopper.
Detailed description of the invention
The preferred technical solution of the present invention is described in detail below in conjunction with accompanying drawing.
As shown in the figure, titanium sponge of the present invention, sponge zirconium variable-frequency ventilation cooling system, comprise body of heater 1, the upper end of described body of heater 1 is provided with forced ventilation system, described forced ventilation system comprises frequency conversion fan 2, blast pipe 3, annular collection wind band 4, described annular collection wind band 4 be arranged two at least up and down in parallel, be separately positioned on the interior of body of heater 1, frequency conversion fan 2 is connected to respectively by blast pipe 3 outside each described annular collection wind band 4, air inlet 5 is evenly provided with inside each described annular collection wind band 4, the annular of the air draft for an air draft collection wind band 6 is also provided with below an annular collection wind band 4 of bottom, duct set road 7 is connected with outside described air draft annular collection wind band 6, exhaust outlet 8 is evenly provided with inside described air draft annular collection wind band 6.
Wherein, each described air inlet 5 is all provided with air intake arm 9, each described exhaust outlet 8 is all provided with air exhaust branch pipe 10, in described duct set road 7, arranged outside has heat-insulation layer 11, described duct set road 7 is provided with electrically operated valve 12, blast pipe 3 described in every root is also provided with valve, described valve is electric butterfly valve 13, described electric butterfly valve 13 and frequency conversion fan 2 are controlled by central control system 14, are also provided with at least one circle stopper 15 at the lower semisection of described body of heater 1 madial wall.
Titanium sponge of the present invention, sponge zirconium variable-frequency ventilation cooling system, arrange annular collection wind band and air draft annular collection wind band, make air intake and air-out very smooth and easy under the power of frequency conversion fan.Air intake arm and air exhaust branch pipe have the effect of reinforcing and leading.Electric butterfly valve and frequency conversion fan are controlled by central control system, make the control accuracy of temperature higher.
Titanium sponge of the present invention, sponge zirconium variable-frequency ventilation cooling system, forced ventilation system solves 1, the slow charging rate of radiating rate is low, and radiating rate significantly improves, and TiCl4 charging rate strengthens.The original charging rate of TiCl440 ton need be added for the whole reduction process of 10t/ stove 10t stove to need to add material in 133 hours for 300kg/h, now only need 66 hours for 600kg/h feed time.2, reactant liquor surface temperature can be controlled in ± 5 DEG C meet manufacturing technique requirent completely.3, whole ventilation process achieves automation without the need to manual operation, reduces labor strength and eliminates potential safety hazard.
The course of work of the present invention is: frequency conversion fan enters burner hearth from 18 along the circumferential direction uniform air intake arms after cold wind being sent into annular collection wind band, wind direction flows from bottom to top along the passage between furnace lining inwall and hypomere also steam, pass through 6 air exhaust branch pipes mutually staggered with 18 air intake arms again and enter duct set road, the exhaust outlet of every platform stove is connected with duct set road, discharges workshop to make hot blast.
Wherein intake size programming implantation DCS central control system and TiCl4 charging rate, in-furnace temperature are interlocked, regulated by frequency conversion fan, opening of electric butterfly valve, upper strata blast pipe and lower floor's blast pipe respectively use an electric butterfly valve separate regulation, the hot blast of exhaust outlet passes through plug or two actions of electrically operated valve open and close, and to the corresponding adjustment of hot blast output.Also there is heat-insulation layer outside, duct set road simultaneously, prevents duct set pipeline outer wall temperature too high.If do not use this forced ventilation system, exhaust outlet can be closed completely.
Claims (4)
1. a titanium sponge, sponge zirconium variable-frequency ventilation cooling system, it is characterized in that: comprise body of heater, the upper end of described body of heater is provided with forced ventilation system, described forced ventilation system comprises frequency conversion fan, blast pipe, annular collection wind band, described annular collection wind band be arranged two at least up and down in parallel, be separately positioned on the interior of body of heater, frequency conversion fan is connected to respectively by blast pipe outside each described annular collection wind band, evenly air inlet is provided with inside each described annular collection wind band, the annular of the air draft for an air draft collection wind band is also provided with below an annular collection wind band of bottom, duct set road is connected with outside described air draft annular collection wind band, evenly exhaust outlet is provided with inside described air draft annular collection wind band.
2. titanium sponge, sponge zirconium variable-frequency ventilation cooling system as claimed in claim 1, it is characterized in that: on each described air inlet, air intake arm is all installed, each described exhaust outlet is all provided with air exhaust branch pipe, in described duct set road, arranged outside has heat-insulation layer, and described duct set road is provided with electrically operated valve.
3. titanium sponge, sponge zirconium variable-frequency ventilation cooling system as claimed in claim 1 or 2, it is characterized in that: on blast pipe described in every root, be also provided with valve, described valve is electric butterfly valve, and described electric butterfly valve and frequency conversion fan are controlled by central control system.
4. titanium sponge, sponge zirconium variable-frequency ventilation cooling system as claimed in claim 3, is characterized in that: be also provided with at least one circle stopper at the lower semisection of described furnace body inside wall.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106521156A (en) * | 2016-12-22 | 2017-03-22 | 遵义钛业股份有限公司 | Forced heat dissipation energy-saving device used for titanium sponge reduction production |
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 |
Citations (7)
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JPH0741880A (en) * | 1993-07-26 | 1995-02-10 | Nippon Steel Corp | Cooling method and device for sponge titanium reducing furnace |
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 |
CN103849784A (en) * | 2012-11-28 | 2014-06-11 | 沈阳铝镁设计研究院有限公司 | Distillation retort cooling device and cooling method |
CN203878191U (en) * | 2014-06-20 | 2014-10-15 | 朝阳金达钛业股份有限公司 | Titanium sponge reacting furnace vent pipe structure |
CN204555704U (en) * | 2015-03-20 | 2015-08-12 | 江苏新辉钛锆装备有限公司 | Titanium sponge, sponge zirconium variable-frequency ventilation cooling system |
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2015
- 2015-03-20 CN CN201510123210.4A patent/CN104776722A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH0741880A (en) * | 1993-07-26 | 1995-02-10 | Nippon Steel Corp | Cooling method and device for sponge titanium reducing furnace |
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 |
CN103849784A (en) * | 2012-11-28 | 2014-06-11 | 沈阳铝镁设计研究院有限公司 | Distillation retort cooling device and cooling method |
CN203878191U (en) * | 2014-06-20 | 2014-10-15 | 朝阳金达钛业股份有限公司 | Titanium sponge reacting furnace vent pipe structure |
CN204555704U (en) * | 2015-03-20 | 2015-08-12 | 江苏新辉钛锆装备有限公司 | Titanium sponge, sponge zirconium variable-frequency ventilation cooling system |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106521156A (en) * | 2016-12-22 | 2017-03-22 | 遵义钛业股份有限公司 | Forced heat dissipation energy-saving device used for titanium sponge reduction production |
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 |
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Effective date of registration: 20151216 Address after: 212300, Zhenjiang Jiangsu Danyang outside the South Gate grass economic Park Applicant after: Danyang Xinhui Furnace Manufacturing Co., Ltd. Address before: 212300 Danyang Jiangsu Zhenjiang city outside the South Gate grass economic Park Applicant before: New brightness titanium zirconium Equipment Limited, Jiangsu |
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RJ01 | Rejection of invention patent application after publication |
Application publication date: 20150715 |
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RJ01 | Rejection of invention patent application after publication |