对采用有机粘结剂球团生产DRI产品的评价

以氧化铁皮为原料,采用有机粘结剂“CC”和以皂土为粘结剂,生产球团作对比试验。结果表明:有机粘结剂“CC”和皂土均可降低生球长大速度,提高生球、干球落下和抗压强度,但生产同样质量的球团矿,“CC”的用量只有皂土用量的1/10。且其直接还原铁(DIR)产品质量优于皂土球团。     

铁矿--生物质复合球团还原行为及还原动力学

通过分析生物质合成气气氛下,不同组分复合球团(添加和未添加生物质)的还原速率、还原度、表面微观结构和失重变化规律,对球团中添加生物质的作用机理以及含生物质球团还原过程的限制性环节展开研究.添加生物质的复合球团表面结构比无生物质球团疏松,孔隙率高,有利于后续还原的热质传递,增加产物还原度,降低反应活化能;复合球团的还原以收缩核方式进行,在1123~1323 K温度范围内,界面化学反应是两种球团还原反应的主要控速环节;添加生物质后,有利于界面化学反应的进行,使得球团的还原表观活化能由95.448 kJ·mol-1降低到68.131 kJ·mol-1.     

矿焦混装对软熔带透气性影响的研究

用熔滴实验装置研究了矿、焦层装及混装时矿石软熔层的透气性,发现混装时软熔层的透气性获得大幅度改善。获得改善的原因在于混装时软溶层的结构发生了质的变化。     

Development of carbon composite iron ore micropellets by using the microfines of iron ore and carbon-bearing materials in iron making

Iron ore microfines and concentrate have very limited uses in sintering processes. They are used in pelletization; however, this process is cost intensive. Furthermore, the microfines of non-coking coal and other carbon-bearing materials, e.g., blast-furnace flue dust (BFD) and coke fines, are not used extensively in the metallurgical industry because of operational difficulties and handling problems. In the present work, to utilize these microfines, coal composite iron oxide micropellets (2-6 mm in size) were produced through an innovative technique in which lime and molasses were used as binding materials in the micropellets. The micropellets were subsequently treated with CO₂ or the industrial waste gas to induce the chemical bond formation. The results show that, at a very high carbon level of 22wt% (38wt% coal), the cold crushing strength and abrasion index of the micropellets are 2.5-3 kg/cm2 and 5wt%-9wt%, respectively; these values indicate that the pellets are suitable for cold handling. The developed micropellets have strong potential as a heat source in smelting reduction in iron making and sintering to reduce coke breeze. The micropellets produced with BFD and coke fines (8wt%-12wt%) were used in iron ore sintering and were observed to reduce the coke breeze consumption by 3%-4%. The quality of the produced sinter was at par with that of the conventional blast-furnace sinter.     

唐钢二炼铁厂使用巴西MBR块矿的生产应用

分析了巴西MBR块矿的矿相结构、矿物组成及冶金性能.MBR块矿的各项冶金性能较好,与烧结矿组成的综合炉料在高炉内的同化过程开始温度和结束温度均较高,但同化速度相对减慢.唐钢二炼铁厂的炼铁生产实践结果表明,适当配用MBR块矿,高炉入炉品位上升,矿耗降低,综合焦比下降,铁成本降低,高炉顺行状态良好.MBR块矿在改善高炉综合技术经济指标的过程中起着重要作用.     

氢气还原褐铁矿实验研究与动力学分析

本文旨在研究不同温度下氢气对褐铁矿还原度和还原速率的影响,并以此为基础分析动力学相关问题.通过热重分析深入了解褐铁矿失水状况.使用粒度为8~12 mm褐铁矿焙烧后,分别在750~950℃五个不同温度下使用4 L·min-1 H2进行还原,并分析还原率和还原速率随时间的变化关系.研究发现：随着反应进行,试样还原率逐渐增大,五条还原率曲线在t>28 min后与还原温度排序一致.通过动力学研究计算得反应表观活化能E=15.323 kJ·mol-1,从而确定扩散为还原反应的限制环节.     

高炉铁水降硅的实验研究

从理论上分析了降低铁水中硅含量的三个途径:控制硅源;降低滴落带的高度;增加炉缸渣中的氧化性.在实验室进行了降低铁水中硅含量的实验,得到了铁水中硅含量的影响因素:提高二元碱度有利于降硅;增加渣中氧化物可降低SiO2的活度有利于降硅;Al2O3和SiO2不利于降硅;冶炼时焦炭中SiO2的挥发量随温度的升高而增多,使铁水中硅含量增加;随着滴落带高度的增加,铁水中硅含量不断增加.根据实验室研究针对唐山建龙公司高炉特点提出降低铁水中硅含量的措施,降硅效果明显,铁水中硅的质量分数由原来的0.55%左右降到了0.40%左右.     

Study of a ceramic burner for shaftless stoves

A multi-burner-port annular flameless ceramic burner (MAFCB) of the shaftless stove for blast furnaces was designed. The characteristics of pressure drop, homogeneousness of the flows at burner ports, and distribution of the flows in the chambers and joint were studied by cold model experiments. This type of ceramic burner was successfully applied in 6# blast furnace at Liuzhou Iron & Steel Co. Ltd. (LISC) and this practice proved that it could be used in the hot blast stove and other stoves with a higher efficiency and a higher steadiness of hot blast temperature at 1200℃. With the combustion of blast furnace gas alone, the thermal efficiency was up to 78.95%, saving energy remarkably.     

Reduction of 1-3 mm iron ore by H2 in a fluidized bed

The reduction of 1-3 mm fine powder of iron ore by H₂ was conducted in a lab-fabricated kg class high temperature fluidized bed. The results show that the differential pressure in the fluidized bed, which has small fluctuation with time, increases with the increase of gas flowing velocity. The utilization ratio of gas decreases when the reaction lasts longer time indicating that the reaction is faster at the beginning of reduction and becomes slower in the latter process. The higher the reaction temperature is, the higher the utilization ratio of gas is, but the difference of utilization ratio among the different temperatures becomes smaller with time. The utilization ratio of gas and the metallization ratio can reach 9% and 84% respectively at 750℃ for 20 min, which shows the reduction reaction by H₂ is very fast. The increase of metallization ratio with gas velocity performs quite good linearity, which shows that a higher velocity of reducing gas can be used to improve the productivity of the reactor when H₂ is used as reducing gas. With the increase of charge height, the metallization ratio decreases, but the utilization ratio of gas increases. The reaction temperature can be reduced to 700-750℃ from 800-850℃ when H₂ is used as reducing gas.