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1.
朱仁林  李建立  沈家豪  余岳  朱航宇 《钢铁》2021,56(11):72-77
 KR脱硫渣是KR铁水预处理脱硫工艺的副产品,其磁选后尾渣中CaO质量分数大于50%。可将其用作优质造渣原料返回到转炉炼钢工艺中,降低转炉炼钢的原料消耗。但KR脱硫渣中的硫(w((S))=1.0%~2.5%)成为转炉冶炼循环利用的障碍,直接将其用于转炉冶炼会使钢中的硫含量增加。因此,根据工业KR脱硫渣的化学成分,以合成渣的形式对KR脱硫渣中矿物组成及含硫相的析出行为进行研究,旨在明确KR脱硫渣中各矿物相组成及炉渣中硫的析出行为和赋存状态,为后续通过氧化性气氛有效脱除KR脱硫渣中的硫提供理论参考。采用热力学数据库FactSage 8.0的Equilib模块对CaO-SiO2-CaS-CaF2基熔渣的凝固过程进行模拟,利用XRD、SEM-EDS对合成渣样品的矿物组成及微观形貌进行分析、检测。热力学计算结果表明,CaS的析晶温度为1 320 ℃,低于MeO#1相、MeO#2相及2CaO·SiO2相的析晶温度。炉渣样品的面扫描分析结果表明,在实际凝固过程中,受残余液相黏度增大的影响炉渣中少量硫未能析出形成CaS晶体,则以非晶态的形式赋存在基质相中。KR脱硫渣主要由C3S相、MeO#1相(CaO固溶体)、MeO#2相(MgO固溶体)、基质相和CaS相等矿物组成。炉渣中的硫主要以游离态CaS晶体形式赋存,少量以非晶态硫的形式赋存。炉渣中CaS晶粒主要沿着先析出的高熔点硅酸盐(C3S)相边界析出。  相似文献   

2.
KR脱硫渣中主要成分(CaO)为转炉冶炼的优质造渣原料,但KR脱硫渣中含有质量分数为1.0%~2.5%的硫,直接将其代替活性石灰用作转炉造渣料回用于冶炼工艺会导致钢液增硫。因此,为了实现KR脱硫渣的氧化脱硫,分析渣中硫氧化行为随炉渣中硫含量变化的机理,通过实验室制取KR脱硫渣样品,采用SEM和XRD分析了氧化后炉渣的微观结构、矿物成分,采用红外碳硫分析仪测定了氧化渣样的硫含量。研究表明,在1 693 K,随硫含量增加炉渣脱硫率先增加后减小,炉渣脱硫率均达到80%以上;随硫含量增加氧化渣样中析出的硅酸盐固相质点数逐渐增加。  相似文献   

3.
高硫容量含BaO超低硫钢精炼脱硫渣系   总被引:1,自引:0,他引:1  
通过500g钼丝炉和10kg感应炉进行了顶渣CaO-SiO2-MgO-Al2O3-CaF2渣系和喂线渣CaO-BaO-CaF2渣系在钢-渣平衡状态的硫容量和钢水脱硫试验。结果表明,该顶渣 喂线渣具有高的硫容量(logC5为-1.6~0.5),适用于超低硫钢的精炼脱硫;CaO-BaO-CaF2中BaO/CaO为5/3时,硫的分配系数L5达到极大值,CaO-SiO2-MgO-Al2O3-CaF2渣系的碱度3.1,炉渣指数MI0.31时,硫的平衡分配系数L5最高。  相似文献   

4.
KR脱硫的渣资源化利用有利于促进钢铁企业的绿色化发展.KR脱硫渣中主要成分为CaO,且含有质量分数为1.0%~2.5%的硫,直接将K R脱硫渣回用于冶炼工艺会导致钢液增硫.若能将渣中的硫脱出,可有效促进KR脱硫渣在钢铁冶炼工艺的资源化利用.因此,针对当前KR脱硫渣综合利用存在的问题,总结分析有关CaS氧化过程的热力学和...  相似文献   

5.
KR脱硫渣中主要成分(CaO)为转炉冶炼的优质造渣原料,通过氧化性气氛将渣中硫脱除后可将其用于转炉冶炼.但由于炉渣冷却制度不同,渣中硫的析出行为和赋存状态会发生变化,对炉渣氧化脱硫效果产生影响.基于此,以合成渣的形式探究冷速对KR脱硫渣中硫析出行为的影响,旨在明确KR脱硫渣中硫赋存状态及析出行为与冷却速率的关系,为后续...  相似文献   

6.
为提高KR脱硫渣的资源化利用水平,利用XRF、XRD、SEM+EDS对某厂KR脱硫渣的矿物学特征进行研究,并用热力学软件FactSage对渣中硫的赋存形式及析出规律进行研究。结果表明,采用石灰系脱硫剂的KR脱硫渣,渣中的主要矿物相为钙铝硅酸盐相、硅酸钙相以及尖晶石相。钙铝硅酸盐相为连续延伸的无定形状,表面光滑平坦,无孔隙和裂纹;硅酸钙相为无规则形状,且表面较为粗糙,有较多的孔隙和裂纹;尖晶石相尺寸大小不一,形状多呈不规则多边板形,少量? 欢ㄐ巫础5蔽露雀哂?220℃时,试验KR脱硫渣中的硫会以SO2的形式存在,CaS约在1220℃时开始析出,CaSO4在1160℃时开始析出,约在1100℃时,CaS和CaSO4的析出量不再随温度的降低而变化,且最终渣中析出CaSO4的较CaS高。  相似文献   

7.
杨必文  宋波  郭凯  陈亮 《钢铁钒钛》2019,40(3):88-92
针对攀西地区铁水/半钢预脱硫效果差异的问题,理论分析了脱硫前后炉渣成分以及物相对脱硫的影响。分析结果表明,脱硫后渣中硫含量为高炉渣/提钒渣的4~5倍,脱硫渣中硫以CaS的形式存在,未发现MgS;半钢脱硫渣平均CaO含量较铁水脱硫渣少15%,FeO含量多9%;铁水预脱硫后渣中低熔点物相含量较少,主要是mCaO·nAl_2O_3(1 400℃),半钢脱硫渣中低熔点物相含量较多,主要是FeO(1 369℃)。增加脱硫剂喷入量,可以提高脱硫渣的固硫能力,减少回硫的发生。高炉渣和提钒渣作为顶渣进入预脱硫工序的渣量(以100 t铁水计)均在1~2 t。  相似文献   

8.
硅镇静钢脱硫渣系的实验室研究   总被引:1,自引:0,他引:1  
钢包炉精炼脱硫过程中顶渣起着非常重要的作用.对硅镇静钢冶炼,为防止钢液回铝,特选择不含铝的脱硫合成渣系CaO-SiO2-CaF2,实验室研究结果表明:初渣成分为CaO 66%、SiO2 17%、CaF2 15%、Si 2%的渣系熔化温度最低,化渣最快,脱硫速度最高,0 min就把硫从0.008%降到0.001%,脱硫效率高,能满足高效连铸的要求.  相似文献   

9.
朱仁林  李建立  余岳  朱航宇 《钢铁》2022,57(2):54-62
KR脱硫渣中的CaO是转炉冶炼工艺中重要的造渣原料,将其回用于钢铁冶炼工艺可降低冶金企业的CaO原料消耗,减少企业KR脱硫渣堆积量,节约企业冶炼的经济成本.KR脱硫渣中的2CaO·SiO2 (C2S)在转炉脱磷冶炼过程中可与炉渣中的磷形成稳定的2CaO· SiO2-3CaO· P2O5固溶体,提高磷在渣中的稳定性.将K...  相似文献   

10.
采用高温硅钼炉和常规化学分析法对高硫含量的硅锰合金进行了系列脱硫研究,分析了CaO-BaO-MgOSiO2-CaF2渣系中MgO、CaO、BaO含量的变化对脱硫效果的影响。结果表明:当MgO的质量分数大于8%时,脱硫率会随着MgO含量的增加而升高。用(MgO+CaF2)代替CaO不利于脱硫;用(MgO+CaF2)代替质量分数为0~4%的BaO有利于渣系脱硫,但代替量过多时不利于脱硫。得到了最佳硅锰合金脱硫的渣系,wCaO/wBaO为1.25时脱硫率最高。  相似文献   

11.
 Abstract: CaO-Al2O3-SiO2-CaF2-MgO was selected as the slag system for desulfurization in LF process. The reaction between steel and slag during desulfurization has been simulated by using Factsage software to study the influence of component on the sulfur distribution ratio. In order to research the influence of CaO content, aluminum powder content and its granularity on desulfurization, laboratory experiments have been carried out in a 200 kg inductive furnace. Results showed that the optimal composition of deep desulfurizer is wCaO=64% and aluminium powder 10% with a granularity of 30 μm. Industrial trials showed that the main composition range of final slag in LF process is wCaO=530%-570%, wAl2O3=234%-251%, wSiO2=81%-100%, and wCaF2=32%-47%. The sulfur mass percent in steel is lower than 00008% with a desulfurization rate above 89%. According to the result of industrial production, this desulfurizer could meet the production requirement for ultra-low sulfur steel, of which sulfur mass percent is under 00015%.  相似文献   

12.
In light of the multicomponent dissolution equilibrium during the hydrothermal leaching of LF desulfurization slag, thermodynamic calculations were made and the dissolution equilibrium curves of calcium, aluminum and sulfur were plotted to analyze the interactions between these components and their influence on sulfur leaching. Furthermore, slag leaching experiments were conducted to investigate variation of pH and concentration of major components in the leaching solution. The results show that CaS(s) is easily soluble in water, and when pH>11. 4, CaS(s) dissolves to form Ca(OH)2(s). Use of hydrothermal leaching for sulfur removal from LF desulfurization slag is theoretically feasible. CaSO4(s) is difficult to dissolve and its solubility is always lower than that of CaS(s); therefore, slag oxidation affects negatively sulfur leaching. However, when the pH of the leaching environment is controlled to be above 12. 3, CaSO4(s) is gradually transformed into Ca(OH)2(s). Al2(SO4)3(s) is easily soluble, and it is unlikely that Al will react with sulfur in the solution to form a precipitate. The pH of the leaching solution rises with time and remains at about 12. Calcium concentration in the leaching solution is high, while Al concentration is low. Sulfur concentration in the solution increases with time, and Al in the slag has little effect on sulfur leaching. It is thus concluded that hydrothermal leaching is effective in removing sulfur from LF desulfurization slag.  相似文献   

13.
The desulfurizationcapability,as one of the mosti m-portant indexes of refining slag,has great influence onquality of steel.Desulfurization of molten steel with refi-ning slags has become a focal problemconcerned all overthe world[1-4].However,there weref…  相似文献   

14.
To develop a high-efficiency desulfurizer for the production of pipeline steel with the LD-RH-CC process, the desulfurization efficiency and mechanism of CaO-saturated slag were studied using a vacuum-induction furnace and Si-Mo electric resistance furnace.The results show that the desulfurization ability for slag with a small amount of solid CaO was highly enhanced under conditions of satisfied kinetics.The desulfurization reaction of CaO-saturated slag depended on the liquid slag rather than the solid CaO,as sulfur was not detected inside the solid CaO.The des-ulfurization efficiency of CaO-saturated slag was also influenced by the amount of residual liquid slag and its sulfur absorption ability.The sulfur absorption ability of CaO-CaF2 slag was analyzed to be much higher than that of CaO-Al2 O3-CaF2-(SiO2 )slag.Moreover,the effect of solid CaO on the desulfurization kinetics was evaluated and the ap-plication conditions of CaO-saturated slag were discussed.  相似文献   

15.
The thermodynamic characteristics of desulfurization reaction (CaO)+[S]=(CaS)+[O] is analyzed based on the detailed composition of liquid steel and slag of Steel Plate Hot Commercial (SPHC) in Jiuquan Iron & Steel Corporation(JISC), where the activities of CaO, CaS and Al2O3 in molten slag are calculated by thermodynamic software FactSage for a more accurate result. The critical values of [O%]/[S%] for desulfurization at different temperature is are obtained, typically 0.09 at 1873K, which shows directly that it should deoxidize adequately for obtaining a favorable desulfurization condition. In addition, the thermodynamic analysis indicates that the actual dissolved O is much higher than that of equilibrium calculation which shows Al-O reaction in LF is far away from equilibrium, but it is perfect agreement with the computing results when taking the activity of Al2O3 as 1 that due to the inclusion component in LF is mainly Al2O3. Besides, with the temperature rise, the sulfur partition ratio increases softly meanwhile the reaction between Al and O is limited to a great degree resulting in the increase a dissolved oxygen in liquid steel that decreases the sulfur partition ratio seriously. As a result, the sulfur partition ratio appears to decrease with temperature increase in Al killed steel.  相似文献   

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