CN102304606A - Slag former and slagging method for semisteel steelmaking - Google Patents
Slag former and slagging method for semisteel steelmaking Download PDFInfo
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- 238000009628 steelmaking Methods 0.000 title claims abstract description 102
- 239000002893 slag Substances 0.000 title claims abstract description 93
- 238000000034 method Methods 0.000 title claims abstract description 73
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 131
- 239000010959 steel Substances 0.000 claims abstract description 131
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 79
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 61
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 61
- 239000004571 lime Substances 0.000 claims abstract description 61
- 238000003723 Smelting Methods 0.000 claims abstract description 40
- 239000011419 magnesium lime Substances 0.000 claims abstract description 35
- 238000007664 blowing Methods 0.000 claims abstract description 33
- 239000012535 impurity Substances 0.000 claims abstract description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 24
- 229910052760 oxygen Inorganic materials 0.000 claims description 24
- 239000001301 oxygen Substances 0.000 claims description 24
- 239000010802 sludge Substances 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 18
- 229910052742 iron Inorganic materials 0.000 claims description 10
- 239000002994 raw material Substances 0.000 claims description 8
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 238000010079 rubber tapping Methods 0.000 claims description 3
- 229940103067 oxygen 60 % Drugs 0.000 claims 1
- 229910004298 SiO 2 Inorganic materials 0.000 abstract description 17
- 230000015572 biosynthetic process Effects 0.000 abstract description 17
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 abstract description 11
- 239000000463 material Substances 0.000 abstract description 9
- 241001062472 Stokellia anisodon Species 0.000 abstract description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 44
- 239000000292 calcium oxide Substances 0.000 description 36
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 36
- 239000000395 magnesium oxide Substances 0.000 description 27
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 26
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 17
- 238000002844 melting Methods 0.000 description 13
- 230000008018 melting Effects 0.000 description 13
- 230000000694 effects Effects 0.000 description 12
- 229910052698 phosphorus Inorganic materials 0.000 description 11
- 239000011574 phosphorus Substances 0.000 description 11
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 10
- 239000002245 particle Substances 0.000 description 9
- 229910052717 sulfur Inorganic materials 0.000 description 9
- 239000011593 sulfur Substances 0.000 description 9
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 8
- 229910052720 vanadium Inorganic materials 0.000 description 8
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 8
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 7
- 239000002131 composite material Substances 0.000 description 7
- 235000013980 iron oxide Nutrition 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 4
- 241001417490 Sillaginidae Species 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 4
- 239000011572 manganese Substances 0.000 description 4
- 229910052710 silicon Inorganic materials 0.000 description 4
- 239000010703 silicon Substances 0.000 description 4
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- 238000006477 desulfuration reaction Methods 0.000 description 3
- 230000023556 desulfurization Effects 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229910000746 Structural steel Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 235000010855 food raising agent Nutrition 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- CSJDCSCTVDEHRN-UHFFFAOYSA-N methane;molecular oxygen Chemical compound C.O=O CSJDCSCTVDEHRN-UHFFFAOYSA-N 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- GFNGCDBZVSLSFT-UHFFFAOYSA-N titanium vanadium Chemical compound [Ti].[V] GFNGCDBZVSLSFT-UHFFFAOYSA-N 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 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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Abstract
本发明提供了一种半钢炼钢用造渣剂及半钢炼钢的造渣方法。所述造渣剂包括60%~75%的SiO2、10%~15%的CaO、1%~3%的MgO、7%~15%的FeO、1%~3%的Fe2O3以及少量不可避免的杂质。所述造渣方法包括:采用半钢炼钢用造渣剂、活性石灰和高镁石灰来进行造渣,并恰当控制造渣材料的加入时机和加入量。采用本发明的半钢炼钢用造渣剂及半钢炼钢的造渣方法来冶炼半钢能够克服半钢冶炼时存在的成渣速度慢、脱磷率低的问题,并能够有效地缩短初期渣形成时间和纯吹氧时间,而且提高转炉终点钢水脱磷率。The invention provides a slagging agent for semi-steel steelmaking and a slagging method for semi-steel steelmaking. The slagging agent includes 60%-75% of SiO 2 , 10%-15% of CaO, 1%-3% of MgO, 7%-15% of FeO, 1%-3% of Fe 2 O 3 and Minor unavoidable impurities. The slagging method includes: using a slagging agent for semi-steel making, active lime and high-magnesium lime to make slagging, and properly controlling the timing and amount of adding slagging materials. Using the slag-forming agent for semi-steel and steelmaking of the present invention and the slagging method for semi-steel steelmaking to smelt semi-steel can overcome the problems of slow slagging speed and low dephosphorization rate during semi-steel smelting, and can effectively shorten the The initial slag formation time and pure oxygen blowing time are improved, and the dephosphorization rate of molten steel at the end of the converter is improved.
Description
技术领域 technical field
本发明涉及炼钢技术领域,更具体地讲,涉及一种半钢炼钢用造渣剂及半钢炼钢的造渣方法。The invention relates to the technical field of steelmaking, more specifically, to a slag-forming agent for semi-steel steelmaking and a slagging method for semi-steel steelmaking.
背景技术 Background technique
当使用钒钛磁铁矿资源进行冶炼来生产钢材时,转炉炼钢的主原料是经过专用转炉提钒后的半钢。通常,将含钒铁水经脱硫提钒后得到的钢水称为半钢。在含钒铁水经脱硫提钒后获得的半钢中,碳质量百分含量为3.4%~4.0%,硅、锰等发热成渣元素含量均为痕迹,硫元素质量百分含量控制在0.015%以内,磷元素质量百分含量为0.060%~0.080%。因此,半钢炼钢具有吹炼过程中酸性成渣物质少、渣系组元单一且热量不足等特点,导致半钢炼钢条件下形成初期渣所需时间长,脱磷率低。热量不足的问题可以通过加入提温剂的方法得以解决,但是成渣速度慢、脱磷率低及冶炼时间偏长的问题,一直是半钢炼钢所存在的突出问题。When vanadium-titanium-magnetite resources are used for smelting to produce steel, the main raw material for converter steelmaking is semi-steel after vanadium extraction in a dedicated converter. Usually, the molten steel obtained after vanadium-containing molten iron is desulfurized and vanadium-extracted is called semi-steel. In the semi-steel obtained after vanadium-containing molten iron is desulfurized and vanadium is extracted, the mass percentage of carbon is 3.4% to 4.0%, the content of exothermic slagging elements such as silicon and manganese are all traces, and the mass percentage of sulfur is controlled at 0.015% Within, the mass percentage content of phosphorus element is 0.060%-0.080%. Therefore, semi-steel steelmaking has the characteristics of less acidic slagging substances, single slag system components and insufficient heat in the blowing process, resulting in a long time for the formation of initial slag under semi-steel steelmaking conditions and a low dephosphorization rate. The problem of insufficient heat can be solved by adding a temperature raising agent, but the problems of slow slagging, low dephosphorization rate and long smelting time have always been prominent problems in semi-steel making.
在现有的技术中,尽管公开了多种转炉炼钢用造渣剂及其制造方法,但是基本上都未能解决上述技术问题。In the prior art, although various slagging agents for converter steelmaking and their manufacturing methods are disclosed, basically none of them can solve the above-mentioned technical problems.
于2000年1月19日公开的第1241637号中国专利申请公开了一种复合造渣剂,该复合造渣剂主要含有(重量百分比)炼钢污泥10%~70%,轻烧镁粉30%~90%。此外,其还可含有硅微粉1%~8%,轻质碳酸钙6%~8%及其它含量大于0%且小于或等于5%的物质。该造渣剂具有熔化快,利用率高,保护炉衬及回收利用炼钢污泥的优点。但是该专利没有说明其具体造渣方法及应用效果;而且从该复合造渣剂的成分可以看出,其主要成分为炼钢污泥球,由于炼钢污泥球具有很强的冷却效果,加之半钢炼钢本来就存在热源不足的问题,所以加入过多的污泥球进行造渣势必会加剧半钢炼钢热源不足的问题,因此,该造渣剂不适合用于半钢冶炼。Chinese Patent Application No. 1241637 published on January 19, 2000 discloses a composite slagging agent, which mainly contains (weight percent) steelmaking sludge 10% to 70%, lightly burned magnesium powder 30% %~90%. In addition, it may also contain 1% to 8% of silicon micropowder, 6% to 8% of light calcium carbonate and other substances whose content is greater than 0% and less than or equal to 5%. The slagging agent has the advantages of fast melting, high utilization rate, protection of furnace lining and recycling of steelmaking sludge. However, the patent does not explain its specific slagging method and application effect; and from the composition of the composite slagging agent, it can be seen that its main component is steelmaking sludge balls. Since steelmaking sludge balls have a strong cooling effect, In addition, there is already a problem of insufficient heat source in semi-steel making, so adding too much sludge balls for slagging will definitely aggravate the problem of insufficient heat source in semi-steel making. Therefore, this slagging agent is not suitable for semi-steel smelting.
于2000年12月27日公开的第1278012号中国专利申请公开了一种用炼钢转炉污泥生产炼钢造渣剂的方法。采用该方法生产出来的炼钢复合渣具有回收利用转炉炼钢污泥、白云石粉等工业废料,降低炼钢成本等特点。但是,该申请主要是阐述了炼钢造渣剂的生产方法,并不涉及使用方法及使用效果,而且考虑到全部采用污泥球造渣半钢温度损失太大,因此,该申请的方法制得的炼钢造渣剂不适合用于半钢冶炼。Chinese Patent Application No. 1278012 published on December 27, 2000 discloses a method for producing a steelmaking slagging agent from steelmaking converter sludge. The steelmaking composite slag produced by the method has the characteristics of recycling converter steelmaking sludge, dolomite powder and other industrial wastes, reducing steelmaking costs and the like. However, this application mainly expounds the production method of steelmaking slagging agent, and does not involve the use method and effect of use, and considering that the temperature loss of semi-steel is too large to use sludge balls to make slag, therefore, the method of this application makes The obtained steelmaking slagging agent is not suitable for semi-steel smelting.
于2009年10月5日在期刊《炼钢》上发表的名称为“利用钢渣制备造渣剂的成型实验研究”的文献,公开了一种采用冷压团成型工艺进行钢渣制备造渣剂的成型方法,并考察了粘结剂用量,配水量和成型压力对压团力学性能的影响。该造渣剂同时具有熔点低、化渣快、脱除钢中有害物质能力强的特点。但是该文献中所生产的造渣剂主要成分为CaO,并且重在研究造渣剂的各项性能,没有对造渣剂的使用效果进行工业验证。The document titled "Experimental Research on the Forming of Slagging Agents Prepared by Using Steel Slag" published in the journal "Steelmaking" on October 5, 2009, discloses a method of preparing slag-forming agents from steel slags using the cold-pressed ball forming process. Forming method, and the influence of the amount of binder, the amount of water and the forming pressure on the mechanical properties of the briquetting was investigated. The slagging agent also has the characteristics of low melting point, fast slagging and strong ability to remove harmful substances in steel. However, the main component of the slagging agent produced in this document is CaO, and the research focuses on the various properties of the slagging agent, and there is no industrial verification of the use effect of the slagging agent.
于2000年11月30日在期刊《钢铁钒钛》上发表的名称为“攀钢炼钢复合造渣剂的研制及应用”的文献,公开了一种根据半钢炼钢的特点设计出的造渣剂,并通过对比试验验证了复合造渣剂主要成分为(重量百分比)SiO2(47.30%)、Al2O3(7.58%)、CaO(11.66%)、MnO(7.67%)时初期渣形成时间为4.97min,较对比试验炉次能缩短初期渣形成时间0.73min,同时使用该造渣剂具有较好的脱磷脱硫能力。但是,从该文献中复合造渣剂的试验效果来看,初期渣形成时间偏长,渣中自由氧化钙含量仍然偏高,说明初期渣没有很好的熔化,仍有提升冶金效果的空间。On November 30, 2000, the document titled "Development and Application of Panzhihua Steelmaking Composite Slagging Agent" published in the journal "Iron and Steel Vanadium Titanium" disclosed a kind of slagging agent designed according to the characteristics of semi-steelmaking. slagging agent, and verified by comparative tests that the main components of the composite slagging agent are (weight percent) SiO 2 (47.30%), Al 2 O 3 (7.58%), CaO (11.66%), MnO (7.67%) when the initial stage The slag formation time is 4.97min, which can shorten the initial slag formation time by 0.73min compared with the comparative test furnace. At the same time, the use of this slagging agent has better dephosphorization and desulfurization ability. However, judging from the test results of the composite slagging agent in this document, the initial slag formation time is relatively long, and the free calcium oxide content in the slag is still relatively high, indicating that the initial slag is not melted well, and there is still room for improving the metallurgical effect.
发明内容 Contents of the invention
针对现有技术存在的不足,本发明的目的之一在于解决上述现有技术中的一个或多个问题。本发明提供了一种半钢炼钢用造渣剂及半钢炼钢的造渣方法,使用本发明能够缩短初期渣形成时间和纯吹氧时间,并能够有效地解决半钢冶炼时成渣慢、脱磷率低的问题,而且提高了半钢冶炼的脱磷效率。In view of the deficiencies in the prior art, one purpose of the present invention is to solve one or more problems in the above prior art. The invention provides a slagging agent for semi-steel making and a slag-making method for semi-steel making. Using the invention can shorten the initial slag formation time and pure oxygen blowing time, and can effectively solve the problem of slag formation during semi-steel smelting slow and low dephosphorization rate, and improve the dephosphorization efficiency of semi-steel smelting.
本发明的一方面提供了一种半钢炼钢用造渣剂。所述造渣剂按重量百分比计包括60%~75%的SiO2、10%~15%的CaO、1%~3%的MgO、7%~15%的FeO、1%~3%的Fe2O3以及少量不可避免的杂质。所述造渣剂按重量百分比计的粒度组成可以为:粒度为15mm~35mm的占95%以上,粒度小于5mm的少于5%。One aspect of the present invention provides a slagging agent for semi-steel making. The slagging agent comprises 60%-75% of SiO 2 , 10%-15% of CaO, 1%-3% of MgO, 7%-15% of FeO, 1%-3% of Fe 2 O 3 and a small amount of unavoidable impurities. The particle size composition of the slagging agent in terms of weight percentage may be: more than 95% of the slagging agent has a particle size of 15 mm to 35 mm, and less than 5% of the particle size is less than 5 mm.
本发明的另一方面提供了一种半钢炼钢的造渣方法。所述造渣方法包括:在转炉冶炼半钢时采用如上所述的半钢炼钢用造渣剂、活性石灰和高镁石灰来进行造渣,在吹炼开始后将所述造渣剂一次性加入全部加入转炉,而将活性石灰和高镁石灰分两批加入转炉,其中,第一批加入的活性石灰和高镁石灰与所述造渣剂同时加入转炉。Another aspect of the present invention provides a slagging method for semi-steel making. The slagging method includes: using the above-mentioned slagging agent for semi-steelmaking, active lime and high-magnesium lime when the converter smelts semi-steel, and using the slagging agent once after blowing starts The active lime and high-magnesia lime are added into the converter in two batches, wherein the first batch of active lime and high-magnesia lime is added to the converter at the same time as the slagging agent.
本发明的又一方面提供了一种半钢炼钢的造渣方法。所述造渣方法包括:在转炉冶炼半钢时采用如上所述的半钢炼钢用造渣剂、活性石灰和高镁石灰来进行造渣,在吹炼开始后将由所述造渣剂、活性石灰和高镁石灰组成的造渣原料分两批加入转炉。Another aspect of the present invention provides a slagging method for semi-steel making. The slag-making method includes: using the above-mentioned slag-forming agent for semi-steelmaking, active lime and high-magnesium lime to carry out slagging when the converter smelts semi-steel, and after the blowing starts, the slag-forming agent, The slagging raw materials composed of active lime and high magnesium lime are added to the converter in two batches.
与现有技术相比,本发明的有益效果在于能够克服在用含钒铁水脱硫提钒后的半钢进行冶炼时存在的成渣速度慢、脱磷率低的问题,并能够有效地缩短初期渣形成时间和纯吹氧时间,而且提高转炉终点钢水脱磷率。Compared with the prior art, the beneficial effect of the present invention is that it can overcome the problems of slow slagging and low dephosphorization rate when smelting semi-steel with vanadium-containing molten iron after desulfurization and vanadium extraction, and can effectively shorten the initial stage. The slag formation time and pure oxygen blowing time are improved, and the dephosphorization rate of molten steel at the end of the converter is improved.
具体实施方式 Detailed ways
在下文中,将结合示例性实施例来详细描述本发明的半钢炼钢用造渣剂和半钢炼钢的造渣方法。在本发明中,如果没有例外的表述,则所有固态和液态物质(例如,造渣剂、活性石灰、高镁石灰、炼钢用污泥球以及钢或钢水中的硫元素和磷元素等)的百分数均为重量百分数,所有气态物质(例如,氧气)的百分数均为体积百分数。Hereinafter, the slagging agent for semi-steel and steelmaking and the slagging method for semi-steel and steelmaking of the present invention will be described in detail with reference to exemplary embodiments. In the present invention, if there is no exception, all solid and liquid substances (for example, slagging agent, active lime, high magnesium lime, sludge balls for steelmaking, and sulfur and phosphorus elements in steel or molten steel, etc.) All percentages are by weight, and all percentages of gaseous substances (eg, oxygen) are by volume.
根据本发明第一方面的半钢炼钢用造渣剂按重量百分比计包括60%~75%的SiO2、10%~15%的CaO、1%~3%的MgO、7%~15%的FeO、1%~3%的Fe2O3以及少量不可避免的杂质。所述造渣剂按重量百分比计的粒度组成可以为:粒度为15mm~35mm的占95%以上,粒度小于5mm的少于5%。本发明的造渣剂含有较高的SiO2,半钢由于硅含量为痕迹,硅氧化期并不能形成大量的SiO2促进化渣,而造渣剂中较高的SiO2在冶炼初期可与CaO形成熔点较低的硅酸盐,加速石灰的溶解,促进化渣。同时造渣剂中含有15%左右的铁的氧化物也可加速石灰的溶解,两个主要成分共同促进了炉渣的熔化,缩短了初期渣形成时间。如果造渣剂中SiO2含量过高,则会使初期炉渣碱度过低,或消耗更多的石灰以达到适合的碱度;如造渣剂中SiO2含量过低,则没有明显的促进化渣的作用。如果铁的氧化物(例如,炼钢污泥球)含量过高,则会使得半钢温降过大,如果铁的氧化物含量过低,则不利于化渣。将造渣剂的粒度保持在15mm~35mm之间主要是为了当将其加入转炉后,能够使其较快的熔化,如果粒度过细或呈粉状,加入过程粉尘过大,同时将其加入转炉后可能会形成一层石灰粉铺在钢液面上或形成石灰跎,影响石灰的熔化从而延长化渣时间;如果造渣剂的粒度大于35mm,则其熔化速度降低。According to the first aspect of the present invention, the slagging agent for semi-steel making steel includes 60% to 75% of SiO 2 , 10% to 15% of CaO, 1% to 3% of MgO, 7% to 15% FeO, 1% to 3% Fe 2 O 3 and a small amount of unavoidable impurities. The particle size composition of the slagging agent in terms of weight percentage may be: more than 95% of the slagging agent has a particle size of 15 mm to 35 mm, and less than 5% of the particle size is less than 5 mm. The slagging agent of the present invention contains relatively high SiO 2 , because the silicon content of semi-steel is a trace, a large amount of SiO 2 cannot be formed during the silicon oxidation period to promote slagging, and the relatively high SiO 2 in the slagging agent can be combined with CaO forms silicate with a lower melting point, which accelerates the dissolution of lime and promotes slag melting. At the same time, about 15% iron oxide contained in the slagging agent can also accelerate the dissolution of lime. The two main components together promote the melting of slag and shorten the initial slag formation time. If the SiO 2 content in the slagging agent is too high, the initial slag alkalinity will be too low, or consume more lime to achieve a suitable alkalinity; if the SiO 2 content in the slagging agent is too low, there will be no obvious promotion The role of slag. If the content of iron oxides (for example, steelmaking sludge balls) is too high, the temperature drop of the semi-steel will be too large, and if the content of iron oxides is too low, it is not conducive to slag melting. The main reason to keep the particle size of the slagging agent between 15mm and 35mm is to melt it faster when it is added to the converter. If the particle size is too fine or powdery, the dust will be too large during the addition process, and it will be added to the converter at the same time. Finally, a layer of lime powder may be formed on the molten steel surface or form a lime slag, which will affect the melting of lime and prolong the slagging time; if the particle size of the slagging agent is greater than 35mm, its melting speed will decrease.
根据本发明第二方面的半钢炼钢的造渣方法包括:在转炉冶炼半钢时采用如上所述的半钢炼钢用造渣剂、活性石灰和高镁石灰来进行造渣,在吹炼开始后将所述造渣剂一次性全部加入转炉,而将活性石灰和高镁石灰分两批加入转炉,其中,第一批加入的活性石灰和高镁石灰与所述造渣剂同时加入转炉。所述根据本发明另一方面的半钢炼钢的造渣方法优选地主要适用于生产对钢水中磷、硫含量要求不高(例如,低于0.025%)的钢种。According to the second aspect of the present invention, the slagging method for semi-steelmaking steelmaking includes: when the converter smelts semi-steel, adopt the above-mentioned semi-steelmaking slagging agent, active lime and high-magnesium lime to carry out slagging, After the smelting starts, the slagging agent is added to the converter all at once, and the active lime and high-magnesia lime are added to the converter in two batches, wherein the first batch of active lime and high-magnesia lime is added at the same time as the slagging agent Converter. The slagging method for semi-steel making steelmaking according to another aspect of the present invention is preferably mainly suitable for the production of steel grades that do not require high phosphorus and sulfur content in molten steel (for example, less than 0.025%).
根据本发明第三方面的半钢炼钢的造渣方法包括:在转炉冶炼半钢时采用如上所述的半钢炼钢用造渣剂、活性石灰和高镁石灰来进行造渣,在吹炼开始后将由所述造渣剂、活性石灰和高镁石灰组成的造渣原料分两批加入转炉。所述根据本发明第三方面的半钢炼钢的造渣方法优选地主要适用于采用大渣量冶炼低磷、低硫钢种的工艺,例如,所述造渣方法可用于生产对钢水中磷和硫的含量要求比较低(例如,低于0.01%)的钢种。According to the third aspect of the present invention, the slagging method of semi-steelmaking steelmaking includes: when the converter smelts semi-steel, adopt the above-mentioned semi-steelmaking slagging agent, active lime and high-magnesium lime to carry out slagging, After the smelting starts, the slagging raw materials composed of the slagging agent, active lime and high-magnesia lime are added to the converter in two batches. The slag-making method for semi-steel steelmaking according to the third aspect of the present invention is preferably mainly suitable for the process of smelting low-phosphorus and low-sulfur steels with a large amount of slag. For example, the slag-making method can be used to produce molten steel Steel grades with relatively low phosphorus and sulfur content (eg, less than 0.01%) are required.
在根据本发明第二方面或第三方面的半钢炼钢的造渣方法的一个示例性实施例中,所述造渣剂的加入总量可以符合下述公式:In an exemplary embodiment of the slagging method for semi-steel making according to the second or third aspect of the present invention, the total amount of the slagging agent added may conform to the following formula:
W1=(W2×η1+W3×η4)/[R(η2-η3)]W1=(W2×η 1 +W3×η 4 )/[R(η 2 -η 3 )]
其中,W1为每吨半钢加入的造渣剂重量,单位为Kg/吨半钢;Among them, W1 is the weight of slagging agent added per ton of semi-steel, and the unit is Kg/ton of semi-steel;
W2为每吨半钢加入的活性石灰的重量,单位为Kg/吨半钢;W2 is the weight of active lime added per ton of semi-steel, in Kg/ton of semi-steel;
W3为每吨半钢加入的高镁石灰的重量,单位为Kg/吨半钢;W3 is the weight of high magnesium lime added per ton of semi-steel, in Kg/ton of semi-steel;
R为转炉吹炼终点炉渣要求达到的碱度,R取3.5~4.5;R is the required basicity of slag at the end of converter blowing, and R is 3.5-4.5;
η1为加入的活性石灰中CaO的质量百分数,单位为%;η 1 is the mass percent of CaO in the active lime that adds, and unit is %;
η2为加入的造渣剂中SiO2的质量百分数,单位为%;η 2 is the mass percentage of SiO in the slagging agent that adds, unit is %;
η3为加入的造渣剂中CaO的质量百分数,单位为%;η 3 is the mass percent of CaO in the slagging agent that adds, unit is %;
η4为加入的高镁石灰中CaO的质量百分数,单位为%。η 4 is the mass percentage of CaO in the high magnesium lime added, and the unit is %.
在本发明中,将碱度设置在3.5~4.5的范围内,主要是为了在炉渣具有较好的脱磷、脱硫效率的同时保证炉渣具有一定的粘度,以满足溅渣护炉的需要,如果碱度过高则会导致炉渣粘度大,溅渣时炉渣不能很好的溅到炉衬上以保护炉衬,如果碱度过低则炉渣脱硫、脱磷效率差且炉渣没有一定的粘度,溅在炉衬上的炉渣不能很好的粘在炉衬上,同样起不到溅渣护炉的作用。In the present invention, the basicity is set within the range of 3.5 to 4.5, mainly to ensure that the slag has a certain viscosity while the slag has better dephosphorization and desulfurization efficiency, so as to meet the needs of slag splashing to protect the furnace. If the alkalinity is too high, the viscosity of the slag will be high. When the slag is splashed, the slag cannot splash well on the furnace lining to protect the furnace lining. The slag on the surface cannot be well adhered to the furnace lining, and it also cannot play the role of slag splashing to protect the furnace.
在根据本发明第二方面或第三方面的半钢炼钢的造渣方法的一个示例性实施例中,所述活性石灰的加入总量可以为25~50Kg/吨钢,且所述活性石灰按重量百分比计可以含有超过85%的CaO;所述高镁石灰的加入总量可以为15~25Kg/吨钢,且所述高镁石灰按重量百分比计可以含有45%~55%的CaO和30%~50%的MgO。In an exemplary embodiment of the slagging method for semi-steel making and steelmaking according to the second aspect or the third aspect of the present invention, the total amount of active lime added may be 25-50Kg/ton of steel, and the active lime It may contain more than 85% CaO by weight percentage; the total amount of the high-magnesia lime added may be 15-25Kg/ton of steel, and the high-magnesia lime may contain 45%-55% CaO and 30% to 50% MgO.
在根据本发明第二方面的半钢炼钢的造渣方法的一个示例性实施例中,所述第一批加入的活性石灰的加入量可以占活性石灰总加入量的70%~80%,所述第一批加入高镁石灰的加入量可以占高镁石灰总加入量的65%~75%,并可以将炉渣碱度控制在2~2.5之间,并且当半钢冶炼的吹氧量达到整个半钢冶炼过程中吹入氧气总量的65%~75%时,可以加入第二批活性石灰和高镁石灰。这里,将炉渣碱度控制在2~2.5之间,主要是因为在该碱度区域时具有最好的脱磷效率,当炉渣碱度大于2.5或小于2时,脱磷效率均降低。这里,之所以在半钢冶炼的吹氧量达到整个半钢冶炼过程中吹入氧气总量的65%~75%时加入第二批活性石灰和高镁石灰,是因为此时前期炉渣早已化透,且已经达到最佳脱磷效果,此时加入第二批渣料可进一步促进脱磷并抑制回磷。In an exemplary embodiment of the slagging method for semi-steelmaking steelmaking according to the second aspect of the present invention, the amount of the first batch of active lime added may account for 70% to 80% of the total amount of active lime added, The amount of the first batch of high-magnesia lime added can account for 65% to 75% of the total amount of high-magnesia lime added, and the basicity of the slag can be controlled between 2 and 2.5, and when the oxygen blowing amount of semi-steel smelting When 65% to 75% of the total amount of oxygen blown in during the whole semi-steel smelting process is reached, the second batch of active lime and high-magnesia lime can be added. Here, the basicity of the slag is controlled between 2 and 2.5, mainly because the dephosphorization efficiency is the best in this basicity range. When the basicity of the slag is greater than 2.5 or less than 2, the dephosphorization efficiency decreases. Here, the reason why the second batch of activated lime and high-magnesium lime is added when the amount of oxygen blown in semi-steel smelting reaches 65% to 75% of the total amount of oxygen blown in the entire semi-steel smelting process is because the slag in the early stage has already melted. and the best dephosphorization effect has been achieved, adding the second batch of slag at this time can further promote dephosphorization and inhibit rephosphorization.
在根据本发明第三方面的半钢炼钢的造渣方法的一个示例性实施例中,第一批加入的所述造渣剂的加入量可以占所述造渣剂总加入量的60~70%,第一批加入的活性石灰的加入量可以占活性石灰总加入量的65%~75%,第一批加入的高镁石灰的加入量可以占高镁石灰总加入量的50%~60%,并且当半钢冶炼的吹氧量达到整个半钢冶炼过程中吹入氧气总量的60%~70%时,可以加入第二批造渣原料。In an exemplary embodiment of the slagging method for semi-steelmaking steelmaking according to the third aspect of the present invention, the amount of the slagging agent added in the first batch can account for 60-60% of the total amount of the slagging agent added. 70%, the amount of active lime added in the first batch can account for 65% to 75% of the total amount of active lime added, and the amount of high magnesium lime added in the first batch can account for 50% to 50% of the total amount of high magnesium lime added 60%, and when the amount of oxygen blown in semi-steel smelting reaches 60%-70% of the total amount of oxygen blown in the whole semi-steel smelting process, the second batch of slagging raw materials can be added.
在根据本发明第二方面或第三方面的半钢炼钢的造渣方法的一个示例性实施例中,所述造渣方法还包括在入炉半钢温度大于1350℃且碳含量大于3.60%时,在加入第一批造渣原料后吹炼2min的时间内向转炉内加入4~8Kg/吨钢炼钢用污泥球,所述炼钢用污泥球按重量百分比计含有25wt%~40wt%铁氧化物。这里,所述炼钢用污泥球为转炉炼钢常用的冷却剂,所不同的是本发明中使用的炼钢用污泥球中含有很高含量的铁氧化物。优选地,本发明中使用的炼钢用污泥球按重量百分比计含有11%~20%的CaO、5%~10%的SiO2、5%~10%的MgO、25%~40%的铁氧化物,其余为水分和不可避免的杂质。在本发明的造渣方法中,加入炼钢用污泥球能够起到降低熔池温度,减缓炉内碳氧反应速率,使熔池升温速率不至于过快,并使熔池在低温区(1400℃~1500℃)保持较长的停留时间的作用,从而能够进一步改善前期低温脱磷的效果。In an exemplary embodiment of the slagging method for semi-steel making according to the second or third aspect of the present invention, the slagging method further includes: When adding the first batch of slagging raw materials, add 4-8Kg/ton of steel-making sludge balls to the converter within 2 minutes of blowing, and the steel-making sludge balls contain 25wt%-40wt% by weight % iron oxide. Here, the sludge balls for steelmaking are commonly used coolants for converter steelmaking, but the difference is that the sludge balls for steelmaking used in the present invention contain a very high content of iron oxides. Preferably, the steelmaking sludge balls used in the present invention contain 11% to 20% of CaO, 5% to 10% of SiO 2 , 5% to 10% of MgO, 25% to 40% of Iron oxides, the rest are moisture and unavoidable impurities. In the slagging method of the present invention, adding sludge balls for steelmaking can reduce the temperature of the molten pool, slow down the carbon-oxygen reaction rate in the furnace, so that the temperature rise rate of the molten pool will not be too fast, and the molten pool will be in the low temperature zone ( 1400℃~1500℃) to maintain a longer residence time, which can further improve the effect of low temperature dephosphorization in the early stage.
在根据本发明第二方面或第三方面的半钢炼钢的造渣方法的一个示例性实施例中,所述造渣方法还包括在转炉出钢前,向转炉中加入调渣剂以调节炉渣粘度的调渣操作,从而减少出钢时的下渣量和保证溅渣护炉操作对炉渣粘度的要求。In an exemplary embodiment of the slagging method for semi-steelmaking according to the second aspect or the third aspect of the present invention, the slagging method further includes adding a slagging agent into the converter to adjust the The slag adjustment operation of slag viscosity can reduce the amount of slag during tapping and ensure the requirement of slag viscosity for slag splash protection operation.
以下,将结合实施例和对比例来进一步描述本发明半钢炼钢用造渣剂和半钢炼钢的造渣方法。Hereinafter, the slagging agent for semi-steel making and the slagging method for semi-steel making steel of the present invention will be further described in combination with examples and comparative examples.
实施例1:Example 1:
采用提钒后的半钢冶炼45#优质碳素结构钢,钢水要求磷、硫含量均低于0.025%。将135t半钢兑入120t转炉进行冶炼并采用根据第二方面的半钢炼钢的造渣方法进行冶炼。Use semi-steel after vanadium extraction to smelt 45# high-quality carbon structural steel, and the content of phosphorus and sulfur in molten steel is required to be lower than 0.025%. Mix 135t of semi-steel into a 120t converter for smelting and use the slagging method of semi-steel making steelmaking according to the second aspect for smelting.
入炉半钢成分为:3.5wt%的C,0.042wt%的Mn,0.088wt%的P,0.015wt%的V,0.009wt%的S,Si为痕迹,其余量为Fe。半钢温度为1335℃。采用5孔氧枪进行吹炼,供氧强度为3.1~4.0Nm3/t·min。在开吹的同时加入全部半钢炼钢用造渣剂和第一批的活性石灰和高镁石灰,其中,活性石灰(含有88wt%的CaO)的加入量为20Kg/t半钢,高镁石灰(含有45wt%的CaO和30wt%的MgO)的加入量为10kg/t半钢。半钢炼钢用造渣剂的加入量为8.26kg/t半钢,其成分为:60wt%的SiO2、15wt%的CaO、3wt%的MgO、15wt%的FeO、3wt%的Fe2O3和余量不可避免的杂质。The composition of the semi-steel in the furnace is: 3.5wt% of C, 0.042wt% of Mn, 0.088wt% of P, 0.015wt% of V, 0.009wt% of S, traces of Si, and the rest of Fe. The semi-steel temperature is 1335°C. A 5-hole oxygen lance is used for blowing, and the oxygen supply intensity is 3.1-4.0Nm 3 /t·min. Add all semi-steel steelmaking slag-forming agents and the first batch of active lime and high-magnesium lime at the same time of blowing, wherein, the addition of active lime (containing 88wt% CaO) is 20Kg/t semi-steel , high-magnesium Lime (containing 45wt% CaO and 30wt% MgO) was added in an amount of 10kg/t semi-steel . The amount of slagging agent used for semi-steel making is 8.26kg/t of semi-steel , and its composition is: 60wt% SiO 2 , 15wt% CaO, 3wt% MgO, 15wt% FeO, 3wt% Fe 2 O 3 and the balance of unavoidable impurities.
在吹氧量达到整个半钢冶炼过程中吹入氧气总量的65%时,加入第二批造渣材料,其中,活性石灰(含有88wt%的CaO)的加入量为8Kg/t半钢,高镁石灰(含有45wt%的CaO和30wt%的MgO)的加入量为5kg/t半钢。然后,调渣出钢,出钢时钢水中磷含量为0.07%。When the oxygen blowing amount reaches 65% of the total amount of oxygen blown in the whole semi-steel smelting process, add the second batch of slagging materials, wherein the addition of active lime (containing 88wt% CaO) is 8Kg/t semi-steel , The addition amount of high magnesium lime (containing 45wt% CaO and 30wt% MgO) is 5kg/t semi-steel . Then, the slag is adjusted and the steel is tapped, and the phosphorus content in the molten steel is 0.07% when the steel is tapped.
测得初期渣形成时间为3.01min,终点炉渣中自由氧化钙的含量为7.13wt%,可见炉渣熔化效果良好。并且纯吹氧时间为11.62min,冶炼过程脱磷率为92.05%。It is measured that the initial slag formation time is 3.01min, and the content of free calcium oxide in the final slag is 7.13wt%, which shows that the slag melting effect is good. And the pure oxygen blowing time is 11.62min, and the dephosphorization rate in the smelting process is 92.05%.
实施例2:Example 2:
采用提钒后的半钢冶炼P72LX钢,钢水要求磷、硫含量均低于0.01%。将138t半钢兑入120t转炉进行冶炼并采用根据第三方面的半钢炼钢的造渣方法进行冶炼。The P72LX steel is smelted using the vanadium-extracted semi-steel, and the phosphorus and sulfur content of molten steel are required to be lower than 0.01%. Mix 138t of semi-steel into a 120t converter for smelting and use the slagging method of semi-steel making steelmaking according to the third aspect for smelting.
入炉半钢成分为:3.46wt%的C,0.038wt%的Mn,0.076wt%的P,0.012wt%的V,0.003wt%的S,Si为痕迹,其余量为Fe。半钢温度为1328℃。采用5孔氧枪进行吹炼,供氧强度为3.1~4.0Nm3/t·min。将由半钢炼钢用造渣剂、活性石灰和高镁石灰组成的造渣材料分两批加入转炉。在开吹的同时加入第一批造渣材料,其中,活性石灰(含有86wt%的CaO)的加入量为35Kg/t半钢,高镁石灰(含有55wt%的CaO和50wt%的MgO)的加入量为10kg/t半钢,半钢炼钢用造渣剂的加入量为9.76kg/t半钢,并且半钢炼钢用造渣剂成分为:75wt%的SiO2、10wt%的CaO、1wt%的MgO、7wt%的FeO和1wt%的Fe2O3和余量不可避免的杂质。The composition of the semi-steel in the furnace is: 3.46wt% of C, 0.038wt% of Mn, 0.076wt% of P, 0.012wt% of V, 0.003wt% of S, traces of Si, and the rest of Fe. The semi-steel temperature is 1328°C. A 5-hole oxygen lance is used for blowing, and the oxygen supply intensity is 3.1-4.0Nm 3 /t·min. The slagging material composed of slagging agent for semi-steel making, active lime and high magnesium lime is added to the converter in two batches. Add the first batch of slagging materials while blowing, wherein, the addition of active lime (containing 86wt% of CaO) is 35Kg/t semi-steel , high magnesium lime (containing 55wt% of CaO and 50wt% of MgO) The addition amount is 10kg/t semi-steel , the addition amount of slagging agent for semi-steel steelmaking is 9.76kg/t semi-steel , and the composition of slagging agent for semi-steel steelmaking is: 75wt% SiO 2 , 10wt% CaO , 1wt% of MgO, 7wt% of FeO and 1wt % of Fe2O3 and the balance of unavoidable impurities.
在吹氧量达到整个半钢冶炼过程中吹入氧气总量的60%时,加入第二批造渣材料,其中,活性石灰(含有86wt%的CaO)的加入量为15Kg/t半钢,高镁石灰(含有55wt%的CaO和50wt%的MgO)的加入量为10kg/t半钢,半钢炼钢用造渣剂(其成分与本实施例中第一批中的半钢炼钢用造渣剂相同)的加入量为4.62kg/t半钢。到冶炼终点时,采用调渣剂调整炉渣粘度,并倒掉部分炉渣,终点钢水中磷含量为0.005%,硫含量为0.005%。When the oxygen blowing amount reaches 60% of the total amount of oxygen blown in the whole semi-steel smelting process, add the second batch of slagging materials, wherein the addition of active lime (containing 86wt% CaO) is 15Kg/t semi-steel , The addition of high magnesium lime (containing 55wt% CaO and 50wt% MgO) is 10kg/t semi-steel , semi-steel steelmaking slagging agent (its composition is the same as that of semi-steel steelmaking in the first batch in this embodiment) The same as the slagging agent) is added in an amount of 4.62kg/t semi-steel . At the end of the smelting process, the viscosity of the slag is adjusted with a slag adjusting agent, and part of the slag is poured out. The phosphorus content in the end point molten steel is 0.005%, and the sulfur content is 0.005%.
测得初期渣形成时间为2.38min,终点炉渣中自由氧化钙含量为6.85wt%,纯吹氧时间为11.48min,转炉冶炼过程脱磷率为93.42%。It is measured that the initial slag formation time is 2.38min, the free calcium oxide content in the final slag is 6.85wt%, the pure oxygen blowing time is 11.48min, and the dephosphorization rate in the converter smelting process is 93.42%.
实施例3:Example 3:
采用提钒后的半钢冶炼50优质碳素结构钢,钢水要求磷、硫含量均低于0.025%。将140t半钢兑入120t转炉进行冶炼并采用根据第二方面的半钢炼钢的造渣方法进行冶炼。The semi-steel after vanadium extraction is used to smelt 50 high-quality carbon structural steel, and the phosphorus and sulfur content of molten steel are required to be lower than 0.025%. Mix 140t of semi-steel into a 120t converter for smelting and use the slagging method of semi-steel making steelmaking according to the second aspect for smelting.
入炉半钢成分为:3.63wt%的C,0.048wt%的Mn,0.068wt%的P,0.018wt%的V,0.0010wt%的S,Si为痕迹,其余量为Fe。半钢温度为1360℃。采用5孔氧枪进行吹炼,供氧强度为3.1~4.0Nm3/t·min。在开吹的同时加入全部半钢炼钢用造渣剂和第一批的活性石灰和高镁石灰,其中,活性石灰(含有87wt%的CaO)的加入量为20Kg/t半钢,高镁石灰(含有50wt%的CaO和40wt%的MgO)的加入量为15kg/t半钢。半钢炼钢用造渣剂的加入量为9.06kg/t半钢,其成分为:68wt%的SiO2、13wt%的CaO、2wt%的MgO、11wt%的FeO、2wt%的Fe2O3和余量不可避免的杂质。The composition of the semi-steel in the furnace is: 3.63wt% of C, 0.048wt% of Mn, 0.068wt% of P, 0.018wt% of V, 0.0010wt% of S, traces of Si, and the rest of Fe. The semi-steel temperature is 1360°C. A 5-hole oxygen lance is used for blowing, and the oxygen supply intensity is 3.1-4.0Nm 3 /t·min. Add all semi-steel steelmaking slagging agents and the first batch of active lime and high-magnesium lime at the same time as the blowing is started, wherein the addition of active lime (containing 87wt% CaO) is 20Kg/t semi-steel , high-magnesium Lime (containing 50wt% CaO and 40wt% MgO) was added in an amount of 15kg/t semi-steel . The amount of slagging agent used for semi-steel making is 9.06kg/t of semi-steel , and its composition is: 68wt% SiO 2 , 13wt% CaO, 2wt% MgO, 11wt% FeO, 2wt% Fe 2 O 3 and the balance of unavoidable impurities.
在吹炼1min后加入炼钢用污泥球6Kg/t半钢。该炼钢用污泥球的含有15%的CaO、8%的SiO2、7%的MgO、33%的铁氧化物以及余量水分和不可避免的杂质。在吹氧量达到整个半钢冶炼过程中吹入氧气总量的75%时,加入第二批造渣材料,其中,活性石灰(含有87wt%的CaO)的加入量为10Kg/t半钢,高镁石灰(含有50wt%的CaO和40wt%的MgO)的加入量为5kg/t半钢。然后,调渣出钢,出钢时钢水中磷含量为0.05%。After blowing for 1 minute, add 6Kg/t semi-steel of sludge balls for steelmaking. This sludge ball for steelmaking contains 15% of CaO, 8% of SiO 2 , 7% of MgO, 33% of iron oxide, and the balance of water and unavoidable impurities. When the oxygen blowing amount reaches 75% of the total amount of oxygen blown in the whole semi-steel smelting process, add the second batch of slagging materials, wherein the addition of active lime (containing 87wt% CaO) is 10Kg/t semi-steel , The addition amount of high magnesium lime (containing 50wt% CaO and 40wt% MgO) is 5kg/t semi-steel . Then, the slag is adjusted and the steel is tapped, and the phosphorus content in the molten steel is 0.05% when the steel is tapped.
测得初期渣形成时间为2.87min,终点炉渣中中自由氧化钙的含量为7.05wt%,可见炉渣熔化效果很好。并且纯吹氧时间为11.79min,冶炼过程脱磷率为92.65%。It is measured that the initial slag formation time is 2.87min, and the content of free calcium oxide in the final slag is 7.05wt%, which shows that the slag melting effect is very good. And the pure oxygen blowing time is 11.79min, and the dephosphorization rate in the smelting process is 92.65%.
对比例1:Comparative example 1:
按实施例1的方法进行转炉炼钢,所不同的是转炉造渣材料全部一次加入转炉,且造渣剂的成分和含量不同,采用常用的复合造渣剂,其成分为:49wt%的SiO2、10wt%的CaO、4wt%的MgO、7wt%的FeO、7wt%的Fe2O3、6wt%的Al2O3、3wt%的C以及余量的水分和不可避免的杂质。结果发现,初期渣形成时间为3.89min,终点炉渣中自由终点炉渣中自由氧化钙的含量为8.68wt%,说明炉渣熔化效果不是很好,纯吹氧时间为12.82min,冶炼过程脱磷率为88.39%。Converter steelmaking is carried out according to the method of Example 1, the difference is that the converter slagging materials are all added to the converter at one time, and the composition and content of the slagging agent are different. A commonly used composite slagging agent is used, and its composition is: 49wt% SiO 2. 10wt% of CaO, 4wt% of MgO, 7wt% of FeO, 7wt% of Fe2O3, 6wt% of Al2O3 , 3wt % of C and the balance of moisture and unavoidable impurities. It was found that the initial slag formation time was 3.89min, and the free calcium oxide content in the terminal slag was 8.68wt%, indicating that the slag melting effect was not very good, the pure oxygen blowing time was 12.82min, and the dephosphorization rate in the smelting process was 88.39%.
对比例2:Comparative example 2:
按实施例2的方法进行转炉炼钢,所不同的是第二批造渣材料在吹炼4min(即,吹氧量约为半钢炼钢过程中吹入氧气总量的30%~40%)后加入,且造渣剂的成分不同,该造渣剂的主要成分为:45wt%的SiO2、13wt%的CaO、3wt%的MgO、10wt%的FeO、9wt%的Fe2O3、5wt%的Al2O3、2wt%的C以及余量的水分和不可避免的杂质。结果发现,初期渣形成时间为3.64min,终点炉渣中自由终点炉渣中自由氧化钙的含量为8.52wt%,说明炉渣熔化效果不是很好,纯吹氧时间为12.73min,冶炼过程脱磷率为89.67%。Carry out the converter steelmaking by the method for embodiment 2, difference is that the second batch of slag-forming materials blows 4min (that is, the oxygen blowing amount is about 30%~40% of the total amount of oxygen blown in the semi-steel steelmaking process ), and the composition of the slagging agent is different. The main components of the slagging agent are: 45wt% SiO 2 , 13wt% CaO, 3wt% MgO, 10wt% FeO, 9wt% Fe 2 O 3 , 5wt% of Al 2 O 3 , 2wt% of C and the rest of moisture and unavoidable impurities. It was found that the initial slag formation time was 3.64min, and the free calcium oxide content in the terminal slag was 8.52wt%, indicating that the slag melting effect was not very good, the pure oxygen blowing time was 12.73min, and the dephosphorization rate in the smelting process was 89.67%.
对比例3:Comparative example 3:
按实施例3的方法进行转炉炼钢,所不同的是将降温材料由所述炼钢用污泥球改为废钢,且造渣剂的成分不同,该造渣剂的主要成分为:50wt%的SiO2、12wt%的CaO、4wt%的MgO、11wt%的FeO、10wt%的Fe2O3、3wt%的Al2O3、3wt%的C以及余量的水分和不可避免的杂质。结果发现,初期渣形成时间为3.89min,终点炉渣中自由氧化钙的含量为8.98wt%,说明炉渣熔化效果不是很好,纯吹氧时间为12.86min,冶炼过程脱磷率为86.43%。Converter steelmaking is carried out according to the method of Example 3, the difference is that the cooling material is changed from the sludge ball for steelmaking to steel scrap, and the composition of the slagging agent is different. The main component of the slagging agent is: 50wt% SiO 2 , 12wt% CaO, 4wt% MgO, 11wt% FeO, 10wt% Fe 2 O 3 , 3wt% Al 2 O 3 , 3wt% C and the balance of moisture and unavoidable impurities. It was found that the initial slag formation time was 3.89min, and the free calcium oxide content in the final slag was 8.98wt%, indicating that the slag melting effect was not very good, the pure oxygen blowing time was 12.86min, and the dephosphorization rate during the smelting process was 86.43%.
从以上实施例和对比例可以看出,使用本发明提供的造渣剂及其造渣方法能有效的缩短初期渣形成时间和纯吹氧时间,且能提高转炉脱磷率。It can be seen from the above examples and comparative examples that using the slagging agent and slagging method provided by the present invention can effectively shorten the initial slag formation time and pure oxygen blowing time, and can increase the dephosphorization rate of the converter.
综上所述,采用本发明的半钢炼钢用造渣剂和半钢炼钢的造渣方法来进行半钢炼钢生产,能够克服半钢冶炼时存在的成渣速度慢、脱磷率低的问题,并能够有效地缩短初期渣形成时间和纯吹氧时间,而且提高转炉终点钢水脱磷率。In summary, adopting the slag-forming agent for semi-steel and steelmaking of the present invention and the slagging method for semi-steel steelmaking to carry out semi-steel steelmaking production can overcome the slow slagging speed and dephosphorization rate that exist during semi-steel smelting. It can effectively shorten the initial slag formation time and pure oxygen blowing time, and increase the dephosphorization rate of molten steel at the end of the converter.
尽管上面已经结合一些示例性实施例描述了本发明,但是本领域技术人员应该清楚,在不脱离权利要求所限定的精神和范围的情况下,可以对上述示例性实施例进行修改和改变。Although the present invention has been described above in conjunction with some exemplary embodiments, it should be apparent to those skilled in the art that modifications and changes may be made to the above exemplary embodiments without departing from the spirit and scope defined by the claims.
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| CN106755714A (en) * | 2016-11-24 | 2017-05-31 | 攀钢集团攀枝花钢钒有限公司 | The method that converter carries out double slag process smelting using corundum slag |
| CN107151725A (en) * | 2017-05-09 | 2017-09-12 | 攀钢集团攀枝花钢铁研究院有限公司 | The method that carbon is protected in semisteel smelting dephosphorization |
| CN113088617A (en) * | 2021-04-09 | 2021-07-09 | 攀钢集团攀枝花钢铁研究院有限公司 | Converter steelmaking method |
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