CN104818366A - Ladle slag conglomeration agent prepared by boric sludge - Google Patents
Ladle slag conglomeration agent prepared by boric sludge Download PDFInfo
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- 239000002893 slag Substances 0.000 title claims abstract description 184
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 70
- 239000010802 sludge Substances 0.000 title abstract 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 207
- 229910052742 iron Inorganic materials 0.000 claims abstract description 104
- 239000000843 powder 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 38
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000002994 raw material Substances 0.000 claims abstract description 19
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 15
- 230000000694 effects Effects 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 238000002347 injection Methods 0.000 claims abstract description 5
- 239000007924 injection Substances 0.000 claims abstract description 5
- 238000002360 preparation method Methods 0.000 claims abstract description 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims description 43
- 229910052796 boron Inorganic materials 0.000 claims description 43
- 238000005507 spraying Methods 0.000 claims description 25
- 239000011777 magnesium Substances 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 16
- 229910052593 corundum Inorganic materials 0.000 claims description 14
- 239000010431 corundum Substances 0.000 claims description 14
- 239000012535 impurity Substances 0.000 claims description 13
- 229910052749 magnesium Inorganic materials 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 13
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 10
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 10
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 10
- 239000004571 lime Substances 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 8
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 5
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 5
- 239000004615 ingredient Substances 0.000 claims description 5
- 238000010410 dusting Methods 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims description 4
- 238000007664 blowing Methods 0.000 claims description 3
- 238000005469 granulation Methods 0.000 claims description 2
- 230000003179 granulation Effects 0.000 claims description 2
- 238000010907 mechanical stirring Methods 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims 1
- 230000008901 benefit Effects 0.000 abstract description 5
- 238000005054 agglomeration Methods 0.000 abstract description 4
- 230000002776 aggregation Effects 0.000 abstract description 4
- 238000000227 grinding Methods 0.000 abstract description 2
- 230000003247 decreasing effect Effects 0.000 abstract 2
- 229910001651 emery Inorganic materials 0.000 abstract 1
- 238000009851 ferrous metallurgy Methods 0.000 abstract 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 14
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 11
- 239000011593 sulfur Substances 0.000 description 11
- 229910052717 sulfur Inorganic materials 0.000 description 11
- 230000008569 process Effects 0.000 description 8
- 239000000292 calcium oxide Substances 0.000 description 7
- 235000012255 calcium oxide Nutrition 0.000 description 7
- 239000002699 waste material Substances 0.000 description 7
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 238000005245 sintering Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000378 calcium silicate Substances 0.000 description 2
- 229910052918 calcium silicate Inorganic materials 0.000 description 2
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000009865 steel metallurgy Methods 0.000 description 2
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229910052656 albite Inorganic materials 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910021538 borax Inorganic materials 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 1
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000010436 fluorite Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229940098458 powder spray Drugs 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000004328 sodium tetraborate Substances 0.000 description 1
- 235000010339 sodium tetraborate Nutrition 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
技术领域 technical field
本发明涉及钢铁冶金技术领域,特别涉及一种硼泥制备的铁水包聚渣剂。 The invention relates to the technical field of iron and steel metallurgy, in particular to a molten iron-coated slag agent prepared from boron mud.
背景技术 Background technique
我国多数硼矿石的品位低,以碳碱法提取硼砂后,产生大量废弃硼泥,由于硼泥处理工艺复杂,一直作为弃渣堆积处理,不仅占用大量土地资源,而且硼泥露天堆积对土壤和水资源形成严重的污染,硼泥综合利用问题有待解决。 The grade of most boron ores in our country is low. After extracting borax by carbon-alkali method, a large amount of waste boron mud is produced. Due to the complicated treatment process of boron mud, it has been piled up as waste residue. Water resources are seriously polluted, and the comprehensive utilization of boron mud needs to be solved .
在钢铁冶金领域,铁水喷粉脱硫预处理已经在全国范围内推广;在铁水包内对铁水脱硫以喷吹CaO、Mg粒或CaO+Mg为主,铁水脱硫后,在铁水包内产生较多量的含硫渣需要扒出,但由于脱硫后的铁渣难以聚集成团块,导致扒渣效率低,扒渣时间长,造成一定程度的铁水回硫,因此在扒渣前需要加入扒渣剂对铁渣进行变质处理;现有技术中,中国专利公开号CN 102560000B 和CN 102586516A 都公开了一种由钠长石、萤石、食盐等构成的聚渣剂,通过降低铁渣碱度来改变渣熔点和粘度,形成粘稠的块状渣团,来提高扒渣效果,但是,这类聚渣剂因为降低了渣碱度,对脱硫不利,铁水回硫问题没有得到有效解决;中国专利公开号CN101392309B公开了一种高碱度的聚渣剂,由轻烧白云石85-100%,生石灰 0-15%构成,但该发明的聚渣剂与钙镁喷粉产生的脱硫渣的组分相近,可以有效减少铁水回硫,但是聚渣效果有待进一步提高。 In the field of iron and steel metallurgy, hot metal spray powder desulfurization pretreatment has been promoted nationwide; the desulfurization of molten iron in the ladle is mainly by spraying CaO, Mg particles or CaO+Mg. After the molten iron is desulfurized, a large amount of The sulfur-containing slag needs to be removed, but because the iron slag after desulfurization is difficult to gather into agglomerates, the efficiency of slag removal is low, and the slag removal time is long, resulting in a certain degree of molten iron resulfurization, so it is necessary to add a slag removal agent before slag removal Perform metamorphic treatment on iron slag; in the prior art, Chinese Patent Publication No. CN 102560000B and CN 102586516A both disclose a slag-accumulating agent composed of albite, fluorite, salt, etc., by reducing the alkalinity of iron slag to change The melting point and viscosity of slag form sticky massive slag clusters to improve the slag removal effect. However, this type of slag gathering agent is not good for desulfurization because it reduces the slag alkalinity, and the problem of molten iron resulfurization has not been effectively solved; Chinese patent publication No. CN101392309B discloses a high-basic slag gathering agent, which is composed of lightly burned dolomite 85-100% and quicklime 0-15%, but the composition of the desulfurization slag produced by the slag gathering agent of the invention and calcium magnesium powder spraying Similar, it can effectively reduce the resulfurization of molten iron, but the effect of slag accumulation needs to be further improved.
铁水在铁水包或鱼雷罐内通过喷粉脱硫后,要尽快扒渣以防止铁水回硫,根据喷粉脱硫后铁水包内铁渣的物理化学特征,聚渣剂应当具有高铺展性与快速成渣、聚渣的特征,聚成渣团后要有是适当的烧结强度,并且,密度要低,容易扒出等,而现有技术中的聚渣剂不能同时具有这种特性,现有技术中的酸性聚渣剂,容易实现快速成渣、聚渣,但容易回硫、且渣过粘,扒渣过程铁损增加严重;而现有技术中的碱性聚渣剂,可以防止铁水回硫,但是聚渣成团的效果不理想,渣的烧结强度低,扒渣易散,导致扒渣次数增加,扒渣效率低。 After the molten iron is desulfurized by powder spraying in the ladle or torpedo tank, the slag should be removed as soon as possible to prevent the molten iron from returning to sulfur. The characteristics of slag and slag accumulation must have appropriate sintering strength after being aggregated into slag clusters, and the density should be low and easy to pick out, etc., while the slag gathering agents in the prior art cannot have this characteristic at the same time. The acidic slag gathering agent in the present technology is easy to realize rapid slag formation and slagging, but it is easy to return to sulfur, and the slag is too sticky, and the iron loss increases seriously during the slag removal process; while the basic slag gathering agent in the prior art can prevent the molten iron from returning to the slag. Sulfur, but the effect of agglomeration of slag is not ideal, the sintering strength of slag is low, and the slag is easily scattered, resulting in an increase in the number of slag removal and low efficiency of slag removal.
综上所述,结合铁水包喷粉脱硫后铁渣的成分组成及特性,同时考虑扒渣要求,需要开发一种既能与喷粉脱硫后的铁渣快速成渣、聚渣成团,提高扒渣效率,同时又能防止铁水回硫、减少扒渣次数,降低扒渣铁损等有益目的为一体的新型聚渣剂。 In summary, in combination with the composition and characteristics of iron slag after desulfurization by powder spraying in ladle, and considering the requirements for slag removal, it is necessary to develop a method that can quickly form slag and aggregate slag with iron slag after powder spray desulfurization, and improve It is a new type of slag gathering agent with beneficial purposes such as improving the efficiency of slag removal, preventing resulfurization of molten iron, reducing the number of times of slag removal, and reducing the iron loss of slag removal.
发明内容 Contents of the invention
本发明的目的是:发明一种利用废弃硼泥制备的铁水包聚渣剂,解决现有技术的聚渣剂存在的聚渣效果差、扒渣效率低、铁水回硫及扒渣次数多、扒渣铁损大等问题,同时实现废弃硼泥的再利用,降低扒渣剂生产成本。 The purpose of the present invention is: to invent a kind of slag gathering agent in molten iron prepared by using waste boron mud to solve the problems of poor slag gathering effect, low slag removal efficiency, many times of molten iron resulfurization and slag removal, etc. The problems such as large iron loss during slag removal can be solved, and at the same time, the waste boron mud can be reused to reduce the production cost of slag removal agent.
实现本发明的技术方案是:一种硼泥制备的铁水包聚渣剂,其特征在于:制备铁水包聚渣剂的原料组成按照重量百分数计算为:硼泥 50-65%、硅石 30-40%、刚玉粉 5-10%。 The technical scheme for realizing the present invention is: a molten iron-coated slag agent prepared by boron mud, characterized in that: the raw material composition for preparing molten iron-coated slag agent is calculated according to weight percentage: boron mud 50-65%, silica 30-40% %, corundum powder 5-10%.
其制备方法的特征在于:经过磨粉、配料、混匀和制粒的方法制备,所有原料经干燥后磨粉过40目筛,然后按上述重量百分数称量配料,通过机械搅拌混料后在滚筒内喷雾造粒,成品粒度1-3mm,然后干燥防潮包装即得到成品。 Its preparation method is characterized in that it is prepared by grinding, batching, mixing and granulating, all the raw materials are dried and then pulverized and passed through a 40-mesh sieve, and then the ingredients are weighed according to the above-mentioned weight percentage, and the mixture is mixed by mechanical stirring. Spray granulation in the drum, the particle size of the finished product is 1-3mm, and then dry and moisture-proof package to get the finished product.
本发明的硼泥制备的铁水包聚渣剂,其使用方法的特征在于:在铁水包内进行喷粉脱硫预处理完成后、扒渣前加入铁水包渣层内,加入量为0.8-1.2Kg/t铁;本发明的铁水包聚渣剂,优先适合用于铁水包喷粉脱硫后聚渣,特别是铁水包喷粉脱硫以喷吹CaO粉、CaO粉+Mg粒或纯Mg粒为主时具有最佳效果;对于不采用喷粉预处理的铁水,铁水包内扒渣同样可以采用本发明,在扒渣前1-2分钟加入到铁水包,然后实施机械扒渣。 The slag-aggregating agent in molten iron prepared by boron mud of the present invention is characterized in that its use method is: after the powder spraying desulfurization pretreatment in the molten iron ladle is completed, and before slag removal, it is added into the molten iron slag layer, and the addition amount is 0.8-1.2Kg /t iron; the hot metal slag gathering agent of the present invention is preferably suitable for gathering slag after ladle powder spraying desulfurization, especially ladle powder spraying desulfurization is mainly based on spraying CaO powder, CaO powder+Mg grains or pure Mg grains It has the best effect; for molten iron that does not adopt powder spraying pretreatment, the present invention can also be used for removing slag in the ladle, and it is added to the ladle 1-2 minutes before the slag removal, and then mechanical slag removal is implemented.
为保证本发明的使用效果,对制备本发明的原料特征进行如下限定: In order to guarantee the use effect of the present invention, the raw material characteristics of the present invention are prepared as follows:
所用硼泥的成分(质量百分数)要求为:MgO 41-50%、SiO2 31~40%、Al2O3 5~8%,余量为杂质组分,杂质的含量越低越好。 The composition (mass percentage) of the boron mud used is required to be: MgO 41-50%, SiO 2 31-40%, Al 2 O 3 5-8%, and the balance is impurity components, the lower the impurity content, the better.
所用硅石的成分(质量百分数)要求为:100% >SiO2 >99%,余量为杂质组分,杂质的含量越低越好。 The composition (mass percentage) of the silica used is required to be: 100% >SiO 2 >99%, and the remainder is impurity components, the lower the impurity content, the better.
所用刚玉粉的成分(质量百分数)要求为:100% >Al2O3 >95%,余量为杂质组分,杂质的含量越低越好。 The composition (mass percentage) of the corundum powder used is required to be: 100% >Al 2 O 3 >95%, and the remainder is impurity components, the lower the impurity content, the better.
制备本发明的原料配比的确定根据如下: The determination of the ratio of raw materials for preparing the present invention is based on the following:
硼泥:硼泥的添加比例为(重量份数)50-65%,其配加比例主要根据铁渣聚渣扒渣所要求的性能指标进行确定,生产中可根据喷粉脱硫情况大致确定,其基本原则是采用单纯喷吹石灰脱硫时,聚渣剂中硼泥的配入量取下限,即50%,采用单纯喷镁脱硫时,聚渣剂中硼泥的配入量取上限,即65%,当采用石灰和镁混吹脱硫时,聚渣剂中硼泥的配入量取50-65%的中间值,最佳取值为57%;硼泥与铁渣具有良好的润湿和快速成渣性能,铺展性好,成渣迅速,且渣团具有适当的烧结强度、易于实现渣金分离,降低扒渣带铁,降低扒渣铁损,同时,硼泥与CaO、CaS、MgS以及硅酸钙都具有很好的结合成渣能力,渣团粘度低、密度小,易于拔除,同时会降低铁水回硫;另外,本发明加入较多硼泥,属碱性扒渣剂,不仅对控制回硫有利,而且对包衬耐火材料也具有很好的保护作用。 Boron mud: The addition ratio of boron mud is (parts by weight) 50-65%. The ratio is mainly determined according to the performance indicators required for iron slag accumulation and slag removal. During production, it can be roughly determined according to the situation of powder spraying and desulfurization. The basic principle is that when simple lime injection is used for desulfurization, the amount of boron mud in the slag gathering agent is taken as the lower limit, that is, 50%. 65%, when using lime and magnesium mixed blowing desulfurization, the amount of boron slime in the slag accumulator should be an intermediate value of 50-65%, and the best value is 57%; boron slime and iron slag have good wetting And fast slagging performance, good spreadability, rapid slagging, and the slag group has appropriate sintering strength, easy to realize slag gold separation, reduce slag strip iron, reduce slag iron loss, at the same time, boron mud and CaO, CaS, Both MgS and calcium silicate have good ability to combine into slag. The slag group has low viscosity and low density, which is easy to remove and can reduce the resulfurization of molten iron. In addition, the present invention adds more boron mud, which is an alkaline slag removal agent. Not only is it beneficial to control the sulfur return, but also has a good protective effect on the lining refractory.
硅石:硅石主要用于调节渣的碱度,与硼泥配合使用,通过调整渣碱度,从而调整渣的粘度、熔点以及渣烧结成团聚块性能,并提高硼泥与铁渣的润湿性,有利于快速成渣聚渣结团,有利于扒渣;硅石的加入量30-40%,实际应用中可根据喷粉的种类进行调整,当喷粉采用单一石灰时,聚渣剂中硅石的加入量取上限即40%,当采用单一喷镁脱硫时,聚渣剂中硅石的加入量取下限即30%;当喷粉脱硫采用石灰-镁混吹时,聚渣剂中硅石的配入量取30-40%的中间值,最佳取值为35%。 Silica: Silica is mainly used to adjust the alkalinity of slag. It is used in conjunction with boron mud. By adjusting the alkalinity of slag, it can adjust the viscosity, melting point and performance of slag sintering into agglomerates, and improve the wettability of boron mud and iron slag. , which is conducive to rapid slag formation and slag agglomeration, and is beneficial to slag removal; the amount of silica added is 30-40%, which can be adjusted according to the type of dusting in practical applications. When single lime is used for dusting, the silica in the slag gathering agent The upper limit of the added amount is 40%. When a single magnesium spray is used for desulfurization, the lower limit of the added amount of silica in the slag gathering agent is 30%. The input amount takes the middle value of 30-40%, and the best value is 35%.
刚玉粉:刚玉粉的加入量(重量份数)范围 5-10%,主要目的是调整渣的粘度、熔点以及渣烧结成团聚块性能,实际应用中可根据喷粉的种类进行调整,当喷粉采用单一石灰时,聚渣剂中刚玉粉的加入量取上限即10%,当采用单一喷镁脱硫时,聚渣剂中刚玉粉的加入量取下限即5%;当喷粉脱硫采用石灰-镁混吹时,聚渣剂中刚玉粉的配入量取5-10%的中间值,最佳取值为8%。 Corundum powder: The amount of corundum powder added (parts by weight) ranges from 5-10%. The main purpose is to adjust the viscosity, melting point and agglomeration performance of slag sintering. In practical applications, it can be adjusted according to the type of powder sprayed. When a single lime powder is used, the upper limit of the amount of corundum powder added to the slag gathering agent is 10%. - When magnesium is mixed and blown, the amount of corundum powder in the slag collector should be an intermediate value of 5-10%, and the best value is 8%.
与现有技术相比本发明的主要优点如下: Compared with prior art, main advantage of the present invention is as follows:
(1)、本发明实现了废弃硼泥的再利用,不仅消除了硼泥危害,而且变废为宝,降低了聚渣剂的生产成本中的原料成本50%以上。 (1) The present invention realizes the reuse of waste boron mud, which not only eliminates the hazard of boron mud, but also turns waste into treasure, reducing the cost of raw materials in the production cost of slag accumulator by more than 50%.
(2)、本发明的聚渣剂用于铁水包扒渣或铁水鱼雷罐扒渣,扒渣效率显著提高,主要体现为:采用本发明,扒渣次数减少,扒渣时间缩短,现有技术扒渣次数一般为20-30次,铁渣扒出率达到80%,而采用本发明,扒渣次数15-20次,铁渣拔出率达到95%;另外,扒渣时间缩短30%左右。 (2) The slagging agent of the present invention is used to remove slag from ladles or molten iron torpedo tanks, and the efficiency of slag removal is significantly improved. The number of slag removal is generally 20-30 times, and the iron slag removal rate reaches 80%. However, with the present invention, the slag removal frequency is 15-20 times, and the iron slag removal rate reaches 95%. In addition, the slag removal time is shortened by about 30%. .
(3)、采用本发明的扒渣剂,扒渣剂使用量减少,现有技术的扒渣剂一般使用量为3-5Kg/t铁,采用本发明时,扒渣剂的加入量为0.8-1.2Kg/t。 (3), adopt the slag removal agent of the present invention, the usage amount of the slag removal agent is reduced, the general use amount of the slag removal agent in the prior art is 3-5Kg/t iron, when adopting the present invention, the addition amount of the slag removal agent is 0.8 -1.2Kg/t.
(4)、扒渣过程的铁损减少,现有技术采用一般聚渣剂产品扒渣时的渣中裹铁导致的铁损在3-5kg/t铁,国外先进的扒渣技术渣中裹铁导致的铁损也在1kg/t铁以上,而采用本发明,由于渣铁界面张力增加,渣密度减小,渣金分离更彻底,渣中裹铁导致的铁损可以降低到0.5-0.8kg/t铁的范围。 (4) The iron loss in the slag removal process is reduced. The iron loss caused by the iron coating in the slag when the general slag gathering agent is used in the existing technology is 3-5kg/t iron. The foreign advanced slag removal technology is wrapped in slag. The iron loss caused by iron is also above 1kg/t iron, but with the present invention, since the slag-iron interfacial tension increases, the slag density decreases, the slag-gold separation is more thorough, and the iron loss caused by iron-coated slag can be reduced to 0.5-0.8 The range of kg/t iron.
综上所述,本发明的优点可以归纳为:低生产成本、高效率以及节能降耗,同时实现废弃物再利用,具有显著的社会经济效益。 To sum up, the advantages of the present invention can be summarized as: low production cost, high efficiency, energy saving and consumption reduction, and at the same time realize waste reuse, which has significant social and economic benefits.
具体实施方式 Detailed ways
实施例所用硼泥的平均成分如表1所示。 The average composition of boron mud that embodiment is used is as shown in table 1.
表1 硼泥的平均成份(质量百分数) The average composition of table 1 boron mud (mass percentage)
实施例 1 Example 1
针对铁水预处理喷粉脱硫工艺采用单一喷吹石灰粉脱硫后的铁渣配制本发明的扒渣聚渣剂,聚渣剂的原料组成(重量分数)如下: The slag-removing and slag-gathering agent of the present invention is prepared by using iron slag after desulfurization by single injection of lime powder for the hot metal pretreatment powder spraying desulfurization process. The raw material composition (weight fraction) of the slag-gathering agent is as follows:
硼泥 50%、硅石 40%、刚玉粉 10%。 Boron mud 50%, silica 40%, corundum powder 10%.
所有原料经干燥、磨粉、配料、混匀和制粒的方法制得成品,具体为:所有原料经干燥后磨粉过40目筛,然后按上述重量百分数称量配料,通过圆盘内机械搅拌混料后在滚筒内喷雾造粒,成品粒度1-3mm,然后干燥防潮包装即得到成品。 All raw materials are dried, milled, batched, mixed and granulated to obtain finished products, specifically: all raw materials are dried and ground to pass through a 40-mesh sieve, and then the ingredients are weighed according to the above weight percentage, passed through the mechanical After stirring and mixing, it is sprayed and granulated in the drum, and the particle size of the finished product is 1-3 mm, and then dried and packed in moisture-proof packaging to obtain the finished product.
在100吨铁水包扒渣时采用本发明的产品,具体实用过程为:在铁水包内进行喷粉脱硫预处理完成后、扒渣前加入铁水包渣层,铁水预处理喷吹单一石灰粉,脱硫完成后,加入本发明的铁水包聚渣剂,加入量按照1.0 kg/t铁撒入铁渣层,聚渣剂铺散性好,成渣快,聚渣成团迅速,约1分钟后实施机械扒渣,扒渣次数15次,铁渣的拔出率达到95%,渣中裹铁率经化学分析为0.08 kg/t渣,扒渣前后,铁水硫含量无变化,即不发生铁水回硫现象。 The product of the present invention is used when removing slag from a 100-ton ladle. The specific practical process is as follows: after the powder spraying desulfurization pretreatment in the ladle is completed, the molten iron slag layer is added before the slag removal, and a single lime powder is sprayed on the molten iron pretreatment. After the desulfurization is completed, add the slag-aggregating agent in molten iron of the present invention, and sprinkle it into the iron slag layer according to the amount of 1.0 kg/t iron. Implement mechanical slag removal, the number of times of slag removal is 15 times, the pull-out rate of iron slag reaches 95%, the rate of iron coating in slag is 0.08 kg/t slag by chemical analysis, the sulfur content of molten iron does not change before and after slag removal, that is, no molten iron occurs back sulfur phenomenon.
实施例 2 Example 2
针对铁水预处理喷粉脱硫工艺采用单一喷吹镁脱硫后的铁渣配制本发明的扒渣聚渣剂,聚渣剂的原料组成(重量分数)如下: The slag removal and slag gathering agent of the present invention is prepared by single injection of iron slag after magnesium desulfurization in the powder spraying desulfurization process of molten iron pretreatment. The raw material composition (weight fraction) of the slag gathering agent is as follows:
硼泥 65%、硅石 30%、刚玉粉 5%。 Boron mud 65%, silica 30%, corundum powder 5%.
所有原料经干燥、磨粉、配料、混匀和制粒的方法制得成品,具体为:所有原料经干燥后磨粉过40目筛,然后按上述重量百分数称量配料,通过圆盘内机械搅拌混料后在滚筒内喷雾造粒,成品粒度1-3mm,然后干燥防潮包装即得到成品。 All raw materials are dried, milled, batched, mixed and granulated to obtain finished products, specifically: all raw materials are dried and ground to pass through a 40-mesh sieve, and then the ingredients are weighed according to the above weight percentage, passed through the mechanical After stirring and mixing, it is sprayed and granulated in the drum, and the particle size of the finished product is 1-3 mm, and then dried and packed in moisture-proof packaging to obtain the finished product.
在100吨铁水包扒渣时采用本发明的产品,具体实用过程为:在铁水包内进行喷粉脱硫预处理完成后、扒渣前加入铁水包渣层,铁水预处理喷吹单一金属镁,脱硫完成后,加入本发明的铁水包聚渣剂,加入量按照0.8 kg/t铁撒入铁渣层,聚渣剂铺散性好,成渣快,聚渣成团迅速,约1分钟后实施机械扒渣,扒渣次数12次,铁渣的拔出率达到95%,渣中裹铁率经化学分析为0.10 kg/t渣,扒渣前后,铁水硫含量无变化,即不发生铁水回硫现象。 The product of the present invention is used when removing slag from a 100-ton ladle. The specific practical process is as follows: after the powder spraying desulfurization pretreatment in the ladle is completed, and before the slag removal, the molten iron slag layer is added, and the molten iron pretreatment is sprayed with single metal magnesium. After desulfurization is completed, add the slag gathering agent in molten iron of the present invention, and sprinkle it into the iron slag layer according to the amount of 0.8 kg/t iron. Implement mechanical slag removal, the number of times of slag removal is 12, the extraction rate of iron slag reaches 95%, the rate of iron coating in slag is 0.10 kg/t slag by chemical analysis, the sulfur content of molten iron does not change before and after slag removal, that is, no molten iron occurs back sulfur phenomenon.
实施例 3 Example 3
针对铁水预处理喷粉脱硫工艺采用生石灰-镁混合喷吹脱硫后的铁渣配制本发明的扒渣聚渣剂,聚渣剂的原料组成(重量分数)如下: The slag-removing and slag-gathering agent of the present invention is prepared by using quicklime-magnesium mixed spraying desulfurized iron slag for the pretreatment of molten iron by powder spraying and desulfurization. The raw material composition (weight fraction) of the slag-gathering agent is as follows:
硼泥 57%、硅石 35%、刚玉粉 8%。 Boron mud 57%, silica 35%, corundum powder 8%.
所有原料经干燥、磨粉、配料、混匀和制粒的方法制得成品,具体为:所有原料经干燥后磨粉过40目筛,然后按上述重量百分数称量配料,通过圆盘内机械搅拌混料后在滚筒内喷雾造粒,成品粒度1-3mm,然后干燥防潮包装即得到成品。 All raw materials are dried, milled, batched, mixed and granulated to obtain finished products, specifically: all raw materials are dried and ground to pass through a 40-mesh sieve, and then the ingredients are weighed according to the above weight percentage, passed through the mechanical After stirring and mixing, it is sprayed and granulated in the drum, and the particle size of the finished product is 1-3 mm, and then dried and packed in a moisture-proof package to obtain the finished product.
在100吨铁水包扒渣时采用本发明的产品,具体实用过程为:在铁水包内进行喷粉脱硫预处理完成后、扒渣前加入铁水包渣层,铁水预处理采用喷吹生石灰-镁(生石灰与镁的质量比为1:1)混合喷吹,脱硫完成后,加入本发明的铁水包聚渣剂,加入量按照1.2 kg/t铁撒入铁渣层,聚渣剂铺散性好,成渣快,聚渣成团迅速,约1分钟后实施机械扒渣,扒渣次数15次,铁渣的拔出率达到95%,渣中裹铁率经化学分析为0.06 kg/t渣,扒渣前后,铁水硫含量无变化,即不发生铁水回硫现象。 The product of the present invention is used when removing slag from a 100-ton ladle, and the specific practical process is as follows: After the powder spraying desulfurization pretreatment in the ladle is completed, the molten iron slag layer is added before the slag removal, and the molten iron pretreatment is sprayed with quicklime-magnesium (The mass ratio of quicklime to magnesium is 1:1) mixed and injected, after the desulfurization is completed, add the molten iron-coated slag agent of the present invention, and the amount added is sprinkled into the iron slag layer according to 1.2 kg/t iron, and the slag-accumulated agent is spreadable. Well, the slag is formed quickly, the slag is gathered and formed into agglomerates quickly, and the mechanical slag is removed after about 1 minute. The number of slag removal is 15 times. The extraction rate of iron slag reaches 95%, and the rate of iron coating in slag is 0.06 kg/t according to chemical analysis. Slag, before and after slag removal, the sulfur content of molten iron does not change, that is, the phenomenon of sulfur reversion in molten iron does not occur.
实施例 1-3 制备的覆盖剂的性能与实际使用效果。 The performance and actual use effect of the covering agent prepared in Examples 1-3 .
对于实施例1-3制得的聚渣剂,经熔化性能检测,该聚渣剂熔点在1300-1320℃,在1350℃下的熔化时间为30-45s,表面张力为0.48N/m, 在一般炼钢生铁铁水脱硫预处理后做扒渣剂,与同等条件下采用其他聚渣剂产品的使用效果进行比较,发现使用本发明比采用其他钙硅酸盐或钙铝酸盐材质的覆盖剂效果要好,主要体现为扒渣效率显著提高,扒渣次数减少,扒渣时间缩短,现有技术扒渣次数一般为20-30次,铁渣扒出率达到80%,而采用本发明,扒渣次数15-20次,铁渣拔出率达到95%;另外,扒渣时间缩短30%左右;另外,扒渣剂的原料成本降低,使用量减少,扒渣铁损降低,统计数据显示,原料成本可以降低50%,扒渣剂使用量降低20%以上,特别是铁损减少50%以上,具有显著的社会经济效益。 For the slagging agent prepared in Example 1-3, the melting point of the slagging agent is 1300-1320°C, the melting time at 1350°C is 30-45s, the surface tension is 0.48N/m, and the melting point is 0.48N/m. Generally, after the desulfurization pretreatment of molten iron for steelmaking pig iron, it is used as a slagging agent. Compared with the use effect of other slagging agent products under the same conditions, it is found that the use of the present invention is better than that of other calcium silicate or calcium aluminate covering agents. The effect is better, which is mainly reflected in that the efficiency of slag removal is significantly improved, the number of slag removal is reduced, and the time of slag removal is shortened. The number of times of slag removal in the prior art is generally 20-30 times, and the iron slag removal rate reaches 80%. The number of slag removal times is 15-20 times, and the iron slag extraction rate reaches 95%; in addition, the slag removal time is shortened by about 30%; in addition, the raw material cost of the slag removal agent is reduced, the usage is reduced, and the iron loss of slag removal is reduced. Statistics show that, The cost of raw materials can be reduced by 50%, the amount of slag removal agent can be reduced by more than 20%, especially the iron loss can be reduced by more than 50%, which has significant social and economic benefits.
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