CN206359558U - KR dusts melt desulfurization agitator - Google Patents
KR dusts melt desulfurization agitator Download PDFInfo
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- CN206359558U CN206359558U CN201621443582.1U CN201621443582U CN206359558U CN 206359558 U CN206359558 U CN 206359558U CN 201621443582 U CN201621443582 U CN 201621443582U CN 206359558 U CN206359558 U CN 206359558U
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- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
The utility model belongs to molten iron pretreatment desulfurizing apparatus field, more particularly to a kind of KR dusts melt desulfurization agitator, including bottom is furnished with stirring vane(1)Stirring body;In the stirring vane(1)Level is fixed with first wheel successively for both sides up and down(201)And second wheel hub(202);In agitating shaft(3)Middle part be fixed with jet pipe(4);In the first wheel(201)Inner chamber is laterally fixed with branch pipe(5);The branch pipe(5)Single port and jet pipe(4)Lower port communicate;Branch pipe(5)Another port and first wheel(201)Spout communicate;In agitating shaft(3)Top be fixed with metallic conduction slip ring(8);Metallic conduction slip ring(8)A signal transmission port and jet pipe(4)Connect, its another signal transmission port and power interface(9)Signal transmission port connect.The utility model is simple in construction, and mixing power is strong, and desulfuration efficiency is high.
Description
Technical field
The utility model belongs to molten iron pretreatment desulfurizing apparatus field, more particularly to a kind of KR dusts melt desulfurization agitator.
Background technology
Developed rapidly as modern industry is produced with scientific and technical, the requirement to steel product quality is increasingly improved.For example, being
Steel billet is avoided to produce underbead crack and obtain good surface quality, it is desirable to which the sulfur content of ordinary steel is less than 0.020%;In order to
Make structural steel that there is uniform mechanical performance, it is desirable to which sulfur content is less than 0.010% in steel;In order that oil and natural gas delivery pipe,
Petroleum refining unit steel, offshore production platform steel, cryogenic steel, medium-thickness ship plate steel and aviation steel etc. have anti-hydrogen induced cracking
The impact flexibility of performance, mechanical performance evenly and Geng Gao, silicon steel has good electromagnetic performance, and sheet steel has excellent
Deep drawability etc., it is desirable to which sulfur content is less than 0.005% in steel.It is required that the steel of such low-sulfur, with traditional blast furnace continuous casting steel machine
Smelt iron a converter steelmaking process be difficult production, only before steel-making plus molten iron pre-desulfurization process, steel-making after add
Furnace outer refining process could be produced.Molten iron pre-desulfurization has turned into one of indispensable process of optimization metallurgical production process, it
Continuous casting steel machine can be reduced | the coke ratio and raising productivity ratio of ironmaking, reduce lime consumption amount and quantity of slag of steel-making etc., so as to reduce
Production cost.
Mainly there are KR methods, RS methods and DO methods in mechanical mixing method desulfurization.KR methods were wide cigarette iron institutes of Nippon Steel in 1963
Start to develop, and industrial production is put into nineteen sixty-five.Used later by NKK and Sumitomo Metal Industries etc..Above-mentioned KR methods profit
Molten iron is set to be contacted well with desulfurizing agent with mechanical agitation, desulfuration efficiency is high and stablizes, and can obtain low-sulfur or super-low sulfur iron
Water.But, existing KR methods mechanical stirring device, generally existing stirring force direction is single, and mixing power is not enough, can cause some desulfurization
Agent, does not participate in desulfurization and has just floated in slag, the insufficient effect that desulfurization is not had still in molten iron of some desulfurization products floating
Really, mixing power is weak, causes desulphurization reaction speed slow, desulfuration efficiency is low.
Utility model content
The utility model is intended to overcome the deficiencies in the prior art part and provide a kind of simple in construction, and mixing power is strong, desulfurization
The KR of efficiency high dusts melt desulfurization agitator.
In order to solve the above technical problems, what the utility model was realized in.
Melt desulfurization turbine type agitating device, including bottom are furnished with the stirring body of stirring vane;In the stirring vane
Level is fixed with first wheel and the second wheel hub successively for both sides up and down;Jet pipe is fixed with the middle part of agitating shaft;Institute
State first wheel inner chamber and be laterally fixed with branch pipe;The Single port of the branch pipe is communicated with the lower port of jet pipe;Branch pipe
Another port communicated with the spout of first wheel;Metallic conduction slip ring is fixed with the top of the agitating shaft;The gold
One signal transmission port of category conducting slip ring connects with jet pipe;Another signal transmission port and power supply of the metallic conduction slip ring
The signal transmission port of interface connects;Refractory material protective layer is fixed with the stirring body exterior.
As a kind of preferred scheme, the angle between the surface and first wheel surface of stirring vane described in the utility model
For 33~66 degree.
Further, the utility model can be provided with poke hole on the stirring vane.
The utility model is blown into nitrogen into molten iron by jet pipe(Or other inert gases), mixing power is improved, can also be dropped
The temperature of low agitating device, extends its service life, Sulfur Content in Hot Iron weight content is reduced to target call, realizes molten iron magnesium
Desulfurization is efficient, meets clean steel production needs.The utility model blade straight by being provided with, and surface and the circle of blade
Angle between the upper surface of shape disk body is 30~60 degree, and the blade being obliquely installed can effectively improve stirring efficiency.
Brief description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and detailed description.Protection model of the present utility model
Enclose the statement for being not only limited to following content.
Fig. 1 is overall structure diagram of the present utility model.
In figure:1st, stirring vane;201st, first wheel;202nd, the second wheel hub;3rd, agitating shaft;4th, jet pipe;5th, branch pipe;6、
Refractory material protective layer;7th, poke hole;8th, metallic conduction slip ring;9th, power interface.
Embodiment
As illustrated, melt desulfurization turbine type agitating device, including bottom are furnished with the stirring body of stirring vane 1;Institute
Stating the both sides up and down of stirring vane 1, level is fixed with the wheel hub 202 of first wheel 201 and second successively;At the middle part of agitating shaft 3
It is fixed with jet pipe 4;Branch pipe 5 is laterally fixed with the inner chamber of first wheel 201;The Single port of the branch pipe 5 with
The lower port of jet pipe 4 is communicated;The another port of branch pipe 5 is communicated with the spout of first wheel 201;In the upper of the agitating shaft 3
Portion is fixed with metallic conduction slip ring 8;One signal transmission port of the metallic conduction slip ring 8 connects with jet pipe 4;The metal
Another signal transmission port of conducting slip ring 8 connects with the signal transmission port of power interface 9;Consolidate in the stirring body exterior
Surely it is provided with refractory material protective layer 6.
Angle between the surface and the surface of first wheel 201 of stirring vane 1 described in the utility model is 33~66 degree.This
Utility model is provided with poke hole 7 on the stirring vane 1.It is, in general, that the power distribution of turbine agitator is to turbulent flow arteries and veins
It is dynamic favourable, and propeller mixer is favourable to overall flow.For same type of agitator, in power consumption identical
Under the conditions of, major diameter, the agitator of the slow-speed of revolution, power are mainly consumed in overall flow, are conducive to micromixing.
The utility model is compared with traditional molten iron desulphurization stirring device, it is to avoid carrier gas mixing direction narrow scope, stirring
The not enough shortcoming of intensity, realizes 360 degrees omnidirection injection and stirring in molten iron, and stirring intensity is doubled.
The utility model can be entered by carrier gas blowing desulfurization agent into molten iron by jet pipe and branch pipe, desulfurized effect
One step is strengthened.
The utility model imports electric current, due to accelerating leading for electronics by slipping into molten iron depths in its exit site
Enter or export speed, so as to enhance effect of the potential energy to the chemical component of desulphurization reaction.Bubbles of carrier gas is in desulfurizing agent feed zone
Effectively stirring, exchanges refining process from dispersity while strengthening fluid kinetic exchange process and is converted into active state
Exchange, this helps to whole molten iron space in bag to be attracted to sweetening process, has finally been to speed up desulfuration operations, has protected
The utilization rate for reducing temperature loss and improving desulfurizing agent is demonstrate,proved.
Preferred embodiment of the present utility model is the foregoing is only, the utility model is not limited to, for this
For the technical staff in field, the utility model can have various modifications and variations.It is all it is of the present utility model spirit and principle
Within, any modification, equivalent substitution and improvements made etc. should be included within protection domain of the present utility model.
Claims (3)
- The melt desulfurization agitator 1. a kind of KR dusts, it is characterised in that be furnished with stirring vane including bottom(1)Stirring body; In the stirring vane(1)Level is fixed with first wheel successively for both sides up and down(201)And second wheel hub(202);Stirring Mix axle(3)Middle part be fixed with jet pipe(4);In the first wheel(201)Inner chamber is laterally fixed with branch pipe(5);Institute State branch pipe(5)Single port and jet pipe(4)Lower port communicate;Branch pipe(5)Another port and first wheel(201)'s Spout is communicated;In the agitating shaft(3)Top be fixed with metallic conduction slip ring(8);The metallic conduction slip ring(8)One Signal transmission port and jet pipe(4)Connect;The metallic conduction slip ring(8)Another signal transmission port and power interface(9) Signal transmission port connect;Refractory material protective layer is fixed with the stirring body exterior(6).
- The melt desulfurization agitator 2. KR according to claim 1 dusts, it is characterised in that:The stirring vane(1)Table Face and first wheel(201)Angle between surface is 33~66 degree.
- The melt desulfurization agitator 3. KR according to claim 2 dusts, it is characterised in that:In the stirring vane(1)On Provided with poke hole(7).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201621443582.1U CN206359558U (en) | 2016-12-27 | 2016-12-27 | KR dusts melt desulfurization agitator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621443582.1U CN206359558U (en) | 2016-12-27 | 2016-12-27 | KR dusts melt desulfurization agitator |
Publications (1)
Publication Number | Publication Date |
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CN206359558U true CN206359558U (en) | 2017-07-28 |
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CN201621443582.1U Active CN206359558U (en) | 2016-12-27 | 2016-12-27 | KR dusts melt desulfurization agitator |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106702071A (en) * | 2016-12-27 | 2017-05-24 | 营口东邦冶金设备耐材有限公司 | KR powder spraying melt desulfuration mixer |
-
2016
- 2016-12-27 CN CN201621443582.1U patent/CN206359558U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106702071A (en) * | 2016-12-27 | 2017-05-24 | 营口东邦冶金设备耐材有限公司 | KR powder spraying melt desulfuration mixer |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address |
Address after: 115100 Yingkou Dongbang Environmental Protection Technology Co., Ltd. of Dashiqiao Huancheng Development Zone, Yingkou City, Liaoning Province Patentee after: Yingkou Dong Bang environmental protection Polytron Technologies Inc Address before: 115100 Liaoning Yingkou Dashiqiao Huancheng Development Zone Yingkou Dongbang Metallurgical Equipment Refractory Co., Ltd. Patentee before: Yingkou Dongbang Metallurgical Refractory Co., Ltd. |
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CP03 | Change of name, title or address |