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Recovery of Nickel from Selectively Reduced Laterite Ore by Sulphuric Acid Leaching

机译:硫酸浸出从选择性还原红土矿石中回收镍

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The laterite ore with low nickel content deposits in Indonesia can be expected to be an alternative raw material of iron making due to its high iron content. One of the required processes is the separation of nickel and cobalt from the laterite ore by leaching it with H_2SO_4 at the atmospheric condition. The sample containing 50.88% iron, 0.03% cobalt and 0.30% nickel was selectively reduced with CO/CO_2 mixed gas to obtain metallic nickel and cobalt, as well as magnetite from hematite. Accordingly, in the leaching process metallic nickel and cobalt will be dissolved by controlling the iron dissolving. The effects of various parameters have been examined. These condition include leaching time, temperature (303-343 K), H_2SO_4 concentration (0.005-1.0) mol/l, as well as extraction rate of nickel. The result of the analysis indicated that the influence of selective reduction could speed up the nickel extraction and obstructed the iron dissolution. The extraction rate of nickel was very high for small particle and slower for larger size. The optimal condition of the test was obtained at the leaching temperature of 343 K, 0.05 mol/l H_2SO_4 with a sample lower than 4.0 g/l. In 60 min after the test, about 93 mass% of nickel was extracted from the sample smaller than 44 μm. The nickel extraction would be higher by adding the leaching time. The rate of extraction was chemically controlled and the apparent activation energy was 42.2 kJ/mol. At the end of the leaching process, there was residual solid rich-magnetite and minimal nickel.
机译:印尼镍含量低的红土矿石由于铁含量高,有望成为炼铁的替代原料。所需的方法之一是在大气条件下通过用H_2SO_4浸出将镍和钴从红土矿石中分离出来。用CO / CO_2混合气体选择性还原含50.88%铁,0.03%钴和0.30%镍的样品,以获得金属镍和钴以及赤铁矿的磁铁矿。因此,在浸出过程中,金属镍和钴将通过控制铁的溶解而溶解。已经检查了各种参数的影响。这些条件包括浸出时间,温度(303-343 K),H_2SO_4浓度(0.005-1.0)mol / l以及镍的萃取率。分析结果表明,选择性还原的影响可加快镍的提取速度,并阻碍铁的溶解。对于小颗粒,镍的萃取率非常高,而对于大颗粒,镍的萃取率却很慢。试验的最佳条件是在343 K,0.05 mol / l H_2SO_4的浸出温度下获得的,样品低于4.0 g / l。试验后60分钟,从小于44μm的样品中提取出约93质量%的镍。通过增加浸出时间,镍的提取将更高。化学控制萃取速率,表观活化能为42.2 kJ / mol。浸出过程结束时,残留的固体富磁铁矿和少量镍。

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