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Preparating Arsenic Trioxide with Sulfuric Acid Wet Oxidation

机译:用硫酸湿氧化制备三氧化砷

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The technology of the acidification is adopted to prepare arsenic trioxide (As2O3). With a concentration of 98% of concentrated sulfuric acid and Orpiment made into a certain ratio of the slurry suspension. Arsenic trioxide's content is 99.94%, extraction yield can reach to 98.92%. The optimal conditions is reaction temperature at 120°Cand the reaction time in 2.5 h; the slurry ratio is less than 1/6 and particle size is less than 0.080 mm. Arsenide is a highly toxic substance, but is an indispensable resource for the development of the national economy [1]. At present, the domestic and foreign technology preparation or recovery of arsenic trioxide method, according to the technical features can be divided into two categories [2-3]: a pyrometallurgical treatment after roasting, arsenic vapor sublimation separation with other materials, secondary oxidation with bags and electrostatic dust collection; pyrometallurgical processing arsenic sulfide ore, slag, mature technology, the process is short, but its handling dry state of arsenic trioxide, harm to operating personnel, can easily cause secondary pollution of the environment [4] and high energy consumption, low product purity, arsenic extraction recovery [5]; the other is wet, to use the acid leaching, alkaline leaching or salt leaching processing [6], arsenic acid with sulfur dioxide reduction for arsenic acid,and then further concentrated cooling crystallization of arsenic trioxide. This experiment, the use of concentrated sulfuric acid in place of the dilute sulfuric acid used in the conventional method, the process is relatively simple, low energy consumption, the processing costs are relatively low.
机译:采用酸化的技术制备三氧化砷(As2O3)。浓度为98%的浓硫酸和浆料悬浮液的一定比例。砷三氧化砷的含量为99.94%,提取收益率可达98.92%。最佳条件是120°C的反应温度,反应时间为2.5小时;浆料比小于1/6,粒度小于0.080mm。砷化物是一种剧毒物质,但是国民经济发展的不可或缺的资源[1]。目前,国内外技术准备或累积砷的三氧化锆方法,根据技术特征可分为两类[2-3]:烘焙后的高温冶金治疗,砷蒸气升华与其他材料分离,二次氧化袋子和静电灰尘收集; Pyrome冶金加工砷硫化物矿石,渣,成熟的技术,过程短,但其处理干燥状态砷三氧化砷,对操作人员的伤害,可以容易地引起次要污染的环境[4]和高能耗,低产品纯度,低产品纯度,砷提取恢复[5];另一个是湿的,使用酸浸出,碱性浸出或盐浸出处理[6],砷酸与二氧化硫的硫酸,然后进一步浓缩砷的三氧化砷结晶。本实验,使用浓硫酸代替常规方法中使用的稀硫酸,该过程相对简单,能耗低,加工成本相对较低。

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