CN204237812U - Pretreatment device for simultaneously desulfurizing, desiliconizing and dephosphorizing molten iron - Google Patents
Pretreatment device for simultaneously desulfurizing, desiliconizing and dephosphorizing molten iron Download PDFInfo
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- CN204237812U CN204237812U CN201420765998.XU CN201420765998U CN204237812U CN 204237812 U CN204237812 U CN 204237812U CN 201420765998 U CN201420765998 U CN 201420765998U CN 204237812 U CN204237812 U CN 204237812U
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 188
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 94
- 230000003009 desulfurizing effect Effects 0.000 title abstract description 7
- 239000000843 powder Substances 0.000 claims abstract description 106
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 53
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 53
- 239000001301 oxygen Substances 0.000 claims abstract description 53
- 239000002893 slag Substances 0.000 claims abstract description 43
- 238000006477 desulfuration reaction Methods 0.000 claims abstract description 38
- 230000023556 desulfurization Effects 0.000 claims abstract description 37
- 238000005507 spraying Methods 0.000 claims abstract description 34
- 238000007599 discharging Methods 0.000 claims abstract description 17
- 239000011449 brick Substances 0.000 claims abstract description 12
- 238000005243 fluidization Methods 0.000 claims abstract description 10
- 238000010079 rubber tapping Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000009423 ventilation Methods 0.000 claims description 6
- 239000011819 refractory material Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 32
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract description 22
- 235000011941 Tilia x europaea Nutrition 0.000 abstract description 22
- 239000004571 lime Substances 0.000 abstract description 22
- 239000011777 magnesium Substances 0.000 abstract description 18
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 abstract description 16
- 229910052749 magnesium Inorganic materials 0.000 abstract description 16
- 239000007789 gas Substances 0.000 abstract description 15
- 238000007664 blowing Methods 0.000 abstract description 13
- 238000003723 Smelting Methods 0.000 abstract description 12
- 229910052710 silicon Inorganic materials 0.000 abstract description 10
- 239000010703 silicon Substances 0.000 abstract description 10
- 238000003756 stirring Methods 0.000 abstract description 10
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 9
- 239000002245 particle Substances 0.000 abstract description 9
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 9
- 239000011574 phosphorus Substances 0.000 abstract description 9
- 239000010436 fluorite Substances 0.000 abstract description 5
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 abstract 1
- 230000008030 elimination Effects 0.000 abstract 1
- 238000003379 elimination reaction Methods 0.000 abstract 1
- 239000011812 mixed powder Substances 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 18
- 101100298222 Caenorhabditis elegans pot-1 gene Proteins 0.000 description 15
- 239000008187 granular material Substances 0.000 description 13
- 229910052751 metal Inorganic materials 0.000 description 12
- 239000002184 metal Substances 0.000 description 12
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 11
- 229910052717 sulfur Inorganic materials 0.000 description 10
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 9
- 229910052757 nitrogen Inorganic materials 0.000 description 9
- 239000005864 Sulphur Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- 238000010410 dusting Methods 0.000 description 5
- 239000011593 sulfur Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 4
- 239000012159 carrier gas Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 238000002161 passivation Methods 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 229910052786 argon Inorganic materials 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000006557 surface reaction Methods 0.000 description 2
- 241001062472 Stokellia anisodon Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229940067573 brown iron oxide Drugs 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 235000003599 food sweetener Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229940098458 powder spray Drugs 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000003765 sweetening agent Substances 0.000 description 1
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- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Abstract
The utility model provides a pretreatment device for simultaneously desulfurizing, desiliconizing and dephosphorizing molten iron. The pretreatment device comprises a powder spraying tank, a powder conveying pipeline, a powder spraying gun and a pretreatment device, wherein the powder spraying tank is provided with a fluidization device and a powder distributor, the powder spraying gun is arranged on the side wall of the pretreatment device, the side wall of the pretreatment device is provided with a slag discharging device, and the bottom of the pretreatment device is provided with an iron outlet. The method for simultaneously desulfurizing molten iron and smelting silicon and phosphorus by adopting the pretreatment device comprises the steps of spraying magnesium particles, lime powder and fluorite powder or mixed powder of the lime powder and the magnesium particles to realize powder spraying desulfurization, spraying oxygen by adopting a top-blowing oxygen lance to complete desiliconization and dephosphorization, utilizing bottom-blowing air-permeable brick bottom blowing gas to strengthen stirring, and effectively separating pretreated molten iron from desulfurized slag or dephosphorized slag by using a slag discharge device and an iron outlet. By adopting the pretreatment device, the molten iron can be desulfurized to be below 0.005 percent and dephosphorized to be below 0.02 percent, so that the molten iron can be simultaneously desulfurized, desilicated and dephosphorized, and the technical requirements of the molten iron triple elimination can be met.
Description
Technical field
The utility model relates to the hot metal pretreatment field of steel smelting procedure, is specifically related to the pretreatment unit of the desulfurization simultaneously of a kind of molten iron, desiliconization, dephosphorization.
Background technology
It is the necessary operation of producing the high-quality such as ultralow-sulfur steel, ultra-low phosphoretic steel special steel that hot metal pretreatment three takes off technique, and current molten iron pretreatment desulfurizing technique mainly contains the means such as torpedo tank car powder injection desulphurization, hot metal ladle powder injection desulphurization, KR stirring desulphurization.Torpedo tank car due to freeboard less, desulfuration efficiency and effect are all restricted, and to the utmostly few to adopt.Hot metal ladle powder injection desulphurization and KR stirring desulphurization have been widely used in the production process of iron and steel enterprise, achieve good sweetening effectiveness, can below desulfurization to 0.005%, but be difficult to remove completely due to desulfurization slag, there is serious time sulphur phenomenon, had a strong impact on sweetening effectiveness.
Silicon removal pretreatment of molten iron and dephosphorization technology all carry out under oxidizing atmosphere condition, because the avidity of silicon and oxygen is much larger than the avidity of phosphorus and oxygen, therefore silicon must be taken off to lower level before dephosphorization.Current dephosphorization, desiliconization pretreatment technology mainly contain the means such as the desiliconization of torpedo tank car dephosphorization, the desiliconization of hot metal ladle dephosphorization, converter dephosphorization desiliconization.Torpedo tank car due to freeboard less, stirring intensity is little, have impact on dephosphorization and desiliconization effect, no longer adopts.Pulvis such as hot metal ladle winding-up lime powder, brown iron oxide and Fluorspar Powder etc. can complete dephosphorization of molten iron and desiliconization process, but due to factor restrictions such as hot metal ladle headroom are little and slag making is difficult, dephosphorization thermodynamics and kinetics condition is poor, and dephosphorization rate is lower, and dephosphorization effect is unstable.In order to improve dephosphorization rate, part iron enterprise adopts special dephosphorization converter to carry out hot metal pretreatment, because converter freeboard is large, the thermodynamics and kinetics condition of dephosphorization is better, therefore, in converter, dephosphorization effect is better, but deslagging difficulty, brings the slag being rich in phosphorus in a large number into, there is more serious rephosphorization phenomenon after converter dephosphorization when tapping a blast furnace, and desulfurization, desiliconization and dephosphorization cannot be carried out simultaneously, result of use is also restricted.
Utility model content
In order to make molten iron desulfurization simultaneously, desiliconization, dephosphorization, solve time sulphur, rephosphorization problem after desulfurizing iron, dephosphorization, the purpose of this utility model is the pretreatment unit providing the desulfurization simultaneously of a kind of molten iron, desiliconization, dephosphorization.
Pretreatment unit of the present utility model can utilize in use dust, oxygen blast, the means such as bottom blowing complete desulfurizing iron, desiliconization, dephosphorization in the pretreater of this pretreatment unit, are conducive to the discharge of slag and molten iron after desulfurization, dephosphorization.
In order to achieve the above object, the utility model provides the desulfurization simultaneously of a kind of molten iron, desiliconization, the pretreatment unit of dephosphorization, as shown in Figure 1, this pretreatment unit comprises at least one powder spraying pot 1, at least one duff pipe road 2, at least one powder monitor 3, pretreater 4, the bottom of powder spraying pot 1 is provided with fluidization equipment 5 and powder distributor 6, fluidization equipment 5 is positioned at the top of powder distributor 6, do not tie with the pulvis ensureing in tank and stick together and good fluidity, and meet the steady winding-up of powder injection desulphurization process, the top on duff pipe road 2 is connected to the outlet of powder distributor 6, powder monitor 3 is connected to the end on duff pipe road 2, and powder monitor 3 is arranged on the sidewall of pretreater 4, pretreater 4 is provided with slag discharging device 7 and iron notch 8, iron notch 8 is positioned at the bottom of pretreater 4, slag discharging device 7 is positioned at the sidewall of pretreater 4, the top of pretreater 4 is provided with top blow oxygen lance 9, bottom is provided with bottom-blown air brick 10, top blow oxygen lance 9 end is provided with ventilation channel 11, suction culvert 12 and water return pipeline 13, ventilation channel 11 is for providing desiliconization, oxygen needed for dephosphorizing process oxidizing reaction, suction culvert 12 and water return pipeline 13 lead to water coolant to improve life-span of oxygen lance.
In above-mentioned pretreatment unit, preferably, the quantity of described powder spraying pot 1 is 2 or 3, and the top on described duff pipe road 2 is divided into 2 or 3 branch roads to be connected to the outlet of the powder distributor 6 of 2 or 3 powder spraying pots 1; Or described powder spraying pot 1 is identical with the quantity on duff pipe road 2, is 2 or 3, several powder spraying pot 1 connects duff pipe road 2 respectively.
In above-mentioned pretreatment unit, preferably, the quantity being connected to the powder monitor 3 on same duff pipe road is that 1-3 props up.
In above-mentioned pretreatment unit, preferably, the rifle body of described powder monitor 3 is stainless steel rifle body, and described powder monitor 3 is the powder monitor wrapping up refractory materials around rifle body.
In above-mentioned pretreatment unit, preferably, described pretreater 4 has the body of heater in district of tapping a blast furnace for side mask, its side cross sectional is circular, this district of tapping a blast furnace becomes converter nose shape, and described iron notch 8 is positioned at pretreater 4 and taps a blast furnace the bottom in district, and the bottom of described pretreater 4 is the combination of the different sphere of two radians, as shown in Figure 3, the radian wherein with the part sphere of iron notch 8 is less than the radian of another part sphere.Adopt this bottom construction, can ensure that molten iron can flow out from furnace bottom iron notch after pretreatment smoothly, compared with conventional iron water preprocessor, solve the problem of difficulty of skimming, anti-non-return sulphur, rephosphorization phenomenon.
In above-mentioned pretreatment unit, preferably, the quantity of described bottom-blown air brick 10 is that 3-12 props up.
In above-mentioned pretreatment unit, preferably, described top blow oxygen lance 9 for oxygen supply intensity be 1.2-4.0Nm
3the supersonic speed oxygen rifle of/min/t molten iron.
Adopt molten iron of the present utility model simultaneously desulfurization, desiliconization, dephosphorization pretreatment unit carry out molten iron desulfurization simultaneously, desiliconization, dephosphorization smelting process comprise the following steps:
Step one: desulfurization, open bottom blown gas, prevent bottom-blown air brick from blocking, molten iron is poured in pretreater 4, make the liquid level of molten iron lower than slag discharging device 7, and make powder monitor 3 be positioned at the position of the above 200-800mm of molten iron level, 20 ° of-70 ° of angles are become with molten iron level, opening powder spraying pot 1 makes pulvis through fluidization equipment 5 and powder distributor 6, then dusted by duff pipe road 2 and powder monitor 3 using nitrogen as winding-up carrier gas, the flow that dusts is 5-200kg/min, Sulfur Content in Hot Iron content is taken off to 0.001-0.005%, utilize nitrogen as winding-up carrier gas, sweetening agent in powder spraying pot 1 is jetted in the molten metal in pretreater by duff pipe road 2 and powder monitor 3, utilize the feature that the specific surface area of the violent stirring effect of carrier gas of dusting and pulvis is large, realize the abundant contact of pulvis-molten metal, complete desulphurization reaction, powder monitor 3 nitrogen blowing is made to protect after powder injection desulphurization terminates, open slag discharging device 7, fascinate pretreater 4 about 5 °-10 °, discharge whole desulfurization slag, prevent molten iron from returning sulphur,
Step 2: desiliconization, adds lime, rhombspar as slag making materials in pretreater 4, and nitrogen-blow or oxygen protection powder monitor 3, continue bottom blown gas to strengthen stirring action, open top blow oxygen lance 9 injecting oxygen, oxygen and silicon are combined rapidly and generate SiO
2enter slag, if initial silicon content > 0.6% in molten iron, time then below desiliconization to 0.2%, stop top blow oxygen lance 9 oxygen blast, open slag discharging device 7, pretreater 4 about 5 ° of-10 ° of discharge section slags that fascinate (amount of the part slag of discharge can carry out conventional regulation and control by those skilled in the art), if initial silicon content≤0.6% in molten iron, time then below desiliconization to 0.2%, can discharge section slag or also can not deslagging;
Step 3: dephosphorization, lime is added in pretreater 4, continue nitrogen blowing or oxygen protection powder monitor 3, top blow oxygen lance 9 injecting oxygen is utilized to realize Fast Slag Melting with oxygen jet, and continue to utilize bottom-blown air brick 10 bottom blown gas to strengthen stirring capacity, slag (foamy slag) and molten iron is made fully to have contacted slag-Jin surface reaction dephosphorization, time below dephosphorization to 0.02%, stop oxygen blast, top blow oxygen lance 9 is proposed, open slag discharging device 7, whole dephosphorization slag discharged by the pretreater 4 about 5 °-10 ° that fascinates, prevent in the process of tapping a blast furnace, bringing high phosphorus slag into and cause rephosphorization, then iron notch 8 is opened, by pretreated sulphur, silicon, the molten iron that phosphorus content is low flows in hot metal ladle, deliver to subsequent processing.
In this application, if no special instructions, all percentage compositions (%) are weight percentage.
In above-mentioned smelting process, preferably, the oxygen supply intensity of top blow oxygen lance 9 injecting oxygen is 1.2-4.0Nm
3/ min/t molten iron.The flow of the top blow oxygen lance injecting oxygen in desiliconization, dephosphorization step can be the same or different.
In above-mentioned smelting process, preferably, described bottom blown gas is nitrogen, argon gas or carbon dioxide.Strengthen stirring action by bottom blowing nitrogen, argon gas or carbon dioxide, increase the dynamic conditions of desulfurization, desiliconization, dephosphorization.The air supply intensity of bottom blown gas is 0.02-0.25Nm
3/ min/t molten iron.The flow of the bottom blown gas in desulfurization, desiliconization, dephosphorization step can be the same or different.
In above-mentioned smelting process, preferably, the pulvis of jetting in sweetening process is the combination of one or more in magnesium granules, lime powder and Fluorspar Powder.More preferably, the pulvis of jetting in sweetening process is the mixing powder of lime powder and magnesium granules.
In above-mentioned smelting process, preferably, described magnesium granules is the magnesium granules after Passivation Treatment, its Mg content>=95.0%, S content≤0.002%, moisture≤0.5%, and particle diameter is 0.1-3mm; CaO content>=88.0% of described lime powder, SiO
2content≤2.5%, S content≤0.05%, moisture≤0.5%, activity degree>=280mL/min, particle diameter < 1mm; The CaF of described Fluorspar Powder
2content>=80%, S content≤0.2%, moisture≤0.5%, particle diameter < 1mm.Wherein, the Passivation Treatment of magnesium granules is ordinary skill in the art means, no longer repeats its concrete steps herein.
In above-mentioned smelting process, preferably, when the pulvis of jetting in sweetening process is two or more in magnesium granules, lime powder and Fluorspar Powder, the quantity of described powder spraying pot 1 is 2 or 3, the top on described duff pipe road 2 is divided into 2 or 3 branch roads to be connected to the outlet of the powder distributor 6 of 2 or 3 powder spraying pots 1, in each powder spraying pot 1, a kind of pulvis being housed, opening several powder spraying pot 1 when dusting simultaneously, several pulvis mixes in duff pipe road 2; Or described powder spraying pot 1 is identical with the quantity on duff pipe road 2, is 2 or 3, several powder spraying pot 1 connects duff pipe road 2 respectively, and open several powder spraying pot 1 when dusting, several pulvis sprays in molten iron respectively by duff pipe road 2 simultaneously simultaneously.
In above-mentioned smelting process, preferably, desiliconization and the lime added in dephosphorizing process and above-mentioned lime powder become to be grouped into, activity degree is identical with the requirement of particle diameter.The rhombspar added in desiliconization process is the rhombspar that this area routine adopts.The amount of the lime added in desiliconization process is 2-20kg/t molten iron, and the amount of rhombspar is 1-10kg/t molten iron.The amount of the lime added in dephosphorizing process is 5-20kg/t molten iron.
The pretreatment unit of molten iron of the present utility model desulfurization simultaneously, desiliconization, dephosphorization can be applied in three de-preprocessing process of molten iron desulfurization simultaneously, desiliconization, dephosphorization, also can be applied in the process of the independent desulfurization of molten iron, desiliconization or dephosphorization.Correspondingly, three steps in the smelting process of the desulfurization simultaneously of above-mentioned molten iron, desiliconization, dephosphorization also can be used alone.
Adopt pretreatment unit of the present utility model can realize molten iron desulfurization simultaneously, desiliconization, dephosphorization, can Sulfur Content in Hot Iron content be taken off to 0.001-0.005%, phosphorus takes off to less than 0.02%, high-sulfur after desulfurization, dephosphorization, high phosphorus slag can be discharged from slag discharging device in time, prevent time sulphur, rephosphorization phenomenon after desulfurizing iron, dephosphorization, be applicable to smelt high-quality steel grade.In addition, pretreatment unit of the present utility model also can independent desulfurization, desiliconization or dephosphorization time use.
Accompanying drawing explanation
The structural representation of the pretreatment unit of desulfurization while that Fig. 1 being the molten iron of an embodiment of the present utility model, desiliconization, dephosphorization.
The structural representation of the pretreatment unit of desulfurization while that Fig. 2 being the molten iron of another embodiment of the present utility model, desiliconization, dephosphorization.
Fig. 3 is the bottom construction schematic diagram of the pretreater in pretreatment unit of the present utility model.
Primary clustering nomenclature:
1. powder spraying pot, 2. duff pipe road, 3. powder monitor, 4. pretreater, 5. fluidization equipment, 6. powder distributor, 7. slag discharging device, 8. iron notch, 9. top blow oxygen lance, 10. bottom-blown air brick, 11. ventilation channels, 12. suction culverts, 13. water return pipelines.
Embodiment
In order to there be understanding clearly to technical characteristic of the present utility model, object and beneficial effect, existing following detailed description is carried out to the technical solution of the utility model, but can not be interpreted as to of the present utility model can the restriction of practical range.
Embodiment 1
The present embodiment provides the desulfurization simultaneously of a kind of molten iron, desiliconization, the pretreatment unit of dephosphorization, as shown in Figure 2, this pretreatment unit comprises two powder spraying pots 1, two duff pipe roads 2, four powder monitors 3, a pretreater 4, the bottom of two powder spraying pots 1 is equipped with fluidization equipment 5 and powder distributor 6, fluidization equipment 5 is positioned at the top of powder distributor 6, do not tie with the pulvis ensureing in tank and stick together and good fluidity, and meet the steady winding-up of powder injection desulphurization process, the top on two duff pipe roads 2 is connected to the outlet of the powder distributor 6 of two powder spraying pots 1, the end on each duff pipe road 2 is connected with two powder monitors 3, and powder monitor 3 is arranged on the sidewall of pretreater 4, the rifle body of powder monitor 3 is stainless steel rifle body, refractory materials protection is wrapped up around rifle body, pretreater 4 is provided with slag discharging device 7 and iron notch 8, iron notch 8 is positioned at the bottom of pretreater 4, slag discharging device 7 is positioned at the sidewall of pretreater 4, the top of pretreater 4 is provided with top blow oxygen lance 9, bottom is provided with bottom-blown air brick 10, the quantity of bottom-blown air brick 10 is 4, top blow oxygen lance 9 adopts four hole supersonic spray guns, oxygen supply intensity is 1.5Nm
3/ min/t molten iron, top blow oxygen lance 9 end is provided with ventilation channel 11, suction culvert 12 and water return pipeline 13, ventilation channel 11 is for providing desiliconization, oxygen needed for dephosphorizing process oxidizing reaction, suction culvert 12 and water return pipeline 13 lead to water coolant to improve life-span of oxygen lance, described pretreater 4 has the body of heater in district of tapping a blast furnace for side mask, its side cross sectional is circular, this district of tapping a blast furnace becomes converter nose shape, described iron notch 8 is positioned at pretreater 4 and taps a blast furnace the bottom in district, the bottom of described pretreater 4 is the combination of the different sphere of two radians, as shown in Figure 3, the radian wherein with the part sphere of iron notch 8 is less than the radian of another part sphere.
Embodiment 2
The present embodiment provides the smelting process of the desulfurization simultaneously of a kind of molten iron, desiliconization, dephosphorization, and the pretreatment unit in employing embodiment 1 is to the desulfurization simultaneously of 150 tons of molten iron, desiliconization, dephosphorization, and this smelting process comprises the following steps:
Step one: desulfurization, open bottom blown gas, flow is 270Nm
3/ h, prevent bottom-blown air brick from blocking, molten iron is poured in pretreater 4, make the liquid level of molten iron lower than slag discharging device 7, and make four powder monitors 3 being connected to two duff pipe roads all be positioned at the position of the above 300mm of molten iron level, angle at 45 ° with molten iron level, open the powder spraying pot 1 that lime powder is housed and start lime powder of jetting, make lime powder through fluidization equipment 5 and powder distributor 6, then duff pipe road 2 is passed through using nitrogen as winding-up carrier gas, lime powder speed of dusting is 30kg/min, the winding-up time is 10-15min, lime powder consumption is 3kg/t molten iron, open the powder spraying pot 1 that magnesium granules is housed simultaneously and start blowing magnesium particle, magnesium granules speed of dusting is 6kg/min, the time of spray magnesium granules is 10-13min, magnesium granules consumption is 0.5kg/t molten iron, magnesium granules and lime powder spray respectively by pulverized coal feed pipe 2 and powder monitor 3, Sulfur Content in Hot Iron content is taken off to less than 0.005%, powder monitor 3 nitrogen blowing is made to protect after powder injection desulphurization terminates, open slag discharging device 7, fascinate pretreater 4 about 5 °-10 °, discharge whole desulfurization slag, prevent molten iron from returning sulphur,
Wherein, magnesium granules is the magnesium granules after Passivation Treatment, its Mg content>=95.0%, S content≤0.002%, moisture≤0.5%, and particle diameter is 0.5-2mm; CaO content>=90.0% of lime powder, SiO
2content≤2.0%, S content≤0.05%, moisture≤0.5%, activity degree>=300mL/min, particle diameter < 1mm;
Step 2: desiliconization, adds lime 5kg/t molten iron, rhombspar 3kg/t molten iron as slag making materials in pretreater 4, and nitrogen-blow protection powder monitor 3, continue bottom blown gas to strengthen stirring action, Bottom Blowing Gas Flow Rate is 270Nm
3/ h, open top blow oxygen lance 9 injecting oxygen, oxygen flow is 13000Nm
3/ h, oxygen and silicon are combined rapidly and generate SiO
2enter slag, initial silicon content > 0.6% in the molten iron of this process, thus below desiliconization to 0.2% time, stop top blow oxygen lance 9 oxygen blast, open slag discharging device 7, fascinate pretreater 4 about 5 ° of-10 ° of discharge section slags;
Step 3: dephosphorization, adds lime 8kg/t molten iron in pretreater 4, and continue nitrogen blowing protection powder monitor 3, utilize top blow oxygen lance 9 injecting oxygen, top blow oxygen lance 9 injecting oxygen flow is 12000Nm
3/ h, realizes Fast Slag Melting, and continues to utilize bottom-blown air brick 10 bottom blown gas, and Bottom Blowing Gas Flow Rate is 350Nm
3/ h, strengthens the stirring capacity of dephosphorizing process, makes slag (foamy slag) and molten iron fully contact slag-Jin surface reaction dephosphorization, and time below dephosphorization to 0.02%, stop oxygen blast, propose top blow oxygen lance 9, Bottom Blowing Gas Flow Rate is adjusted to 270Nm
3/ h, open slag discharging device 7, whole dephosphorization slag discharged by the pretreater 4 about 5 °-10 ° that fascinates, prevent in the process of tapping a blast furnace, bringing high phosphorus slag into and cause rephosphorization, then iron notch 8 is opened, the molten iron of pretreated sulphur content < 0.005%, silicone content vestige, phosphorus content < 0.02% is flowed in hot metal ladle, delivers to subsequent processing.
Claims (7)
1. a molten iron desulfurization simultaneously, desiliconization, the pretreatment unit of dephosphorization, it is characterized in that, described pretreatment unit comprises at least one powder spraying pot (1), at least one duff pipe road (2), at least one powder monitor (3), pretreater (4), the bottom of powder spraying pot (1) is provided with fluidization equipment (5) and powder distributor (6), fluidization equipment (5) is positioned at the top of powder distributor (6), the top on duff pipe road (2) is connected to the outlet of powder distributor (6), powder monitor (3) is connected to the end of duff pipe road (2), and powder monitor (3) is arranged on the sidewall of pretreater (4), pretreater (4) is provided with slag discharging device (7) and iron notch (8), iron notch (8) is positioned at the bottom of pretreater (4), slag discharging device (7) is positioned at the sidewall of pretreater (4), the top of pretreater (4) is provided with top blow oxygen lance (9), bottom is provided with bottom-blown air brick (10), top blow oxygen lance (9) end is provided with ventilation channel (11), suction culvert (12) and water return pipeline (13).
2. the pretreatment unit of molten iron according to claim 1 desulfurization simultaneously, desiliconization, dephosphorization, it is characterized in that, the quantity of described powder spraying pot (1) is 2 or 3, and the top of described duff pipe road (2) is divided into 2 or 3 branch roads to be connected to the outlet of the powder distributor (6) of 2 or 3 powder spraying pots (1); Or described powder spraying pot (1) is identical with the quantity of duff pipe road (2), is 2 or 3, several powder spraying pot (1) connects duff pipe road (2) respectively.
3. the pretreatment unit of molten iron according to claim 1 desulfurization simultaneously, desiliconization, dephosphorization, it is characterized in that, the quantity being connected to the powder monitor (3) on same duff pipe road is that 1-3 props up.
4. the pretreatment unit of molten iron according to claim 1 desulfurization simultaneously, desiliconization, dephosphorization, it is characterized in that, the rifle body of described powder monitor (3) is stainless steel rifle body, and described powder monitor (3) is for wrapping up the powder monitor of refractory materials around rifle body.
5. the pretreatment unit of molten iron according to claim 1 desulfurization simultaneously, desiliconization, dephosphorization, it is characterized in that, described pretreater (4) has the body of heater in district of tapping a blast furnace for side mask, its side cross sectional is circular, this district of tapping a blast furnace becomes converter nose shape, described iron notch (8) is positioned at pretreater (4) and taps a blast furnace the bottom in district, the bottom of described pretreater (4) is the combination of the different sphere of two radians, and the radian wherein with the part sphere of iron notch (8) is less than the radian of another part sphere.
6. the pretreatment unit of molten iron according to claim 1 desulfurization simultaneously, desiliconization, dephosphorization, it is characterized in that, the quantity of described bottom-blown air brick (10) is that 3-12 props up.
7. the pretreatment unit of molten iron according to claim 1 desulfurization simultaneously, desiliconization, dephosphorization, is characterized in that, described top blow oxygen lance (9) for oxygen supply intensity be 1.2-4.0Nm
3the supersonic speed oxygen rifle of/min/t molten iron.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104480251A (en) * | 2014-12-05 | 2015-04-01 | 中冶京诚工程技术有限公司 | Pretreatment device for simultaneously desulfurizing, desiliconizing and dephosphorizing molten iron, application and smelting method |
| CN110669921A (en) * | 2019-10-18 | 2020-01-10 | 甘肃酒钢集团宏兴钢铁股份有限公司 | System and method for resourcefully treating steelmaking secondary dedusting ash |
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2014
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104480251A (en) * | 2014-12-05 | 2015-04-01 | 中冶京诚工程技术有限公司 | Pretreatment device for simultaneously desulfurizing, desiliconizing and dephosphorizing molten iron, application and smelting method |
| CN110669921A (en) * | 2019-10-18 | 2020-01-10 | 甘肃酒钢集团宏兴钢铁股份有限公司 | System and method for resourcefully treating steelmaking secondary dedusting ash |
| CN110669921B (en) * | 2019-10-18 | 2023-10-27 | 甘肃酒钢集团宏兴钢铁股份有限公司 | System and method for recycling steelmaking secondary dust removal ash |
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