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Research on the recycling of valuable metals in spent Al_2O_3-based catalyst

机译:Al_2O_3废催化剂中有价金属的回收利用研究

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A new technology was developed to recover multiple valuable elements in the spent Al_2O_3-based catalyst by X-ray phase analysis and exploratory experiments. The experiment results showed: In the condition of roasting temperature of 750 deg C and roasting time of 30 min, mol ratio of Na_2O: Al_2O_3 1.2, the leaching rate of alumina, vanadium and molybdenum in the spent catalyst is 97.2 percent, 95.8 percent and 98.9 percent, respectively. Vanadium and molybdenum in sodium aluminate solution can be recovered by barium hydroxide and barium aluminate, the precipitation rate of vanadium and molybdenum is 94.8 percent and 92.6 percent. Al(OH)_3 is prepared from sodium aluminate solution with carbonation decomposition process, and the purity of Al_2O_3 is 99.9 percent after calcinations, the recovery of alumina can reach 90.6 percent in the whole process. The Ni-Co concentrate was leached by sulfuric acid, a nickel recovery of 98.2 percent and over 98.5 percent cobalt recovery was obtained respectively under the experimental condition of 30 percent (w/w) H_2SO_4, 80 deg C, reaction time 4 h, liquid:solid ratio (8:1) by weight, stirring rate of 800 rpm.
机译:通过X射线相分析和探索性实验,开发了一种新技术来回收废Al_2O_3基催化剂中的多种有价值的元素。实验结果表明:在焙烧温度为750℃,焙烧时间为30 min,Na_2O:Al_2O_3摩尔比为1.2的条件下,废催化剂中氧化铝,钒和钼的浸出率分别为97.2%,95.8%和90.5%。分别为98.9%。用氢氧化钡和铝酸钡可以回收铝酸钠溶液中的钒和钼,钒和钼的沉淀率分别为94.8%和92.6%。由铝酸钠溶液经碳酸分解法制得Al(OH)_3,煅烧后Al_2O_3的纯度为99.9%,整个过程中氧化铝的回收率可达到90.6%。通过硫酸浸提镍钴精矿,在30%(w / w)H_2SO_4、80℃,反应时间4 h,液体的实验条件下,镍的回收率分别为98.2%和98.5%以上的钴回收率。 :固体重量比(8∶1),搅拌速度为800rpm。

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