Study on calcification reduction sodium removal of vanadium extraction tailings by coal-based rotary kiln method
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摘要: 针对提钒尾渣中钠含量高,导致难以返回烧结-高炉流程进行回收利用的问题,提出基于煤基回转窑还原的提钒尾渣钙化还原脱钠技术路线,并在Ø1 m×10 m回转窑中试线进行半工业试验,主要研究了高温段还原温度、白灰配比、入窑吨球焦粉配比、高温还原时间对提钒尾渣脱钠的影响规律,同时对脱钠后球团性能和回转窑结窑情况进行分析。结果表明,在高温段温度为1100~1160 ℃,高温段时间为1.8~2 h,入窑吨球焦粉配比为800~1000 kg,白灰配比为32.5%~41%的条件下,提钒尾渣脱钠率可达到80%以上,吨球焦粉实际消耗量为359 kg。窑内结块物主要由提钒尾渣球团粉末和焦粉灰分粉末组成,结块物呈疏松多孔状,由细颗粒相互粘结构成,窑转动过程会自动掉落,无明显结窑现象。Abstract: In view of the high sodium content in vanadium extraction tailings, which leads to the difficulty of returning to the sintering-blast furnace process for recycling, herein we proposed a calcification reduction sodium removal technology route for vanadium extraction tailings based on coal-based rotary kiln reduction, and conducted a semi-industrial test on a Ø1 m×10 m rotary kiln pilot line. The influence of reduction time in the high temperature section, white ash ratio, into the kiln ton-ball coke ratio and high temperature reduction time on vanadium extraction tailings sodium removal was mainly studied. At the same time, the performance of pellets after desalination and the situation of kiln formation in the rotary kiln were analyzed. Under the conditions of high temperature section temperature of 1100~1160 ℃, high temperature section time of 1.8~2 h, into the kiln ton-ball coke ratio of 800~1000 kg, white ash ratio of 32.5%~41%, the sodium removal rate of vanadium extraction tailings can reach more than 80%, and the coke consumption is 359 kg. The agglomeration in the kiln is mainly composed of vanadium extraction tailings pellet powder and coke ash powder. The agglomeration is loose and porous, consisting of fine particles which are sticky to each other. The agglomeration will fall off automatically during the kiln rotation process, without obvious kiln formation phenomenon.
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表 1 提钒尾渣主要化学成分
Table 1. Main chemical composition of vanadium extraction tailing
% Na2O K2O TFe SiO2 TiO2 Al2O3 CaO MgO V2O5 4.85 0.016 32.32 13.64 11.92 2.78 1.88 1.69 1.34 表 2 脱钠球团主要成分
Table 2. Main composition of desalination pellets
% Na2O K2O MFe TFe SiO2 TiO2 Al2O3 CaO MgO V2O5 0.47 未检出 20.54 24.95 10.44 8.93 2.16 26.88 2.69 1.84 表 3 结窑物关键元素含量
Table 3. Key element content of agglomerate
% 样品 Fe Ca Mg Al Si Na 随窑排出 11.26 9.68 1.58 4.85 6.47 1.39 内壁附着 11.35 9.24 1.95 5.05 7.12 1.11 -
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