首页> 外文期刊>Advanced Powder Technology: The internation Journal of the Society of Powder Technology, Japan >Enhanced recovery of dithionate from desulfurization with pyrolusite system by manganese dioxide anode of spent batteries
【24h】

Enhanced recovery of dithionate from desulfurization with pyrolusite system by manganese dioxide anode of spent batteries

机译:通过锰二氧化碳阳极通过花电池用吡咯岩系统提高二硫酸盐的回收率

获取原文
获取原文并翻译 | 示例
           

摘要

Manganese dithionate is a byproduct, accompanied by the formation of manganese sulfate, of the leaching process of sulfur dioxide (SO2) with pyrolusite. The as-produced MnS2O6 is disadvantageous for recovering MnSO4 by debasing the purity of the MnSO4 product. To obtain the qualified MnSO4 product, removing MnS2O6 from the leaching solution is critical. In this work, the conversion characteristics of MnS2O6 in the H2SO4-MnO2 system were studied. The conversion mechanisms of MnS2O6 were determined by a material balance of sulfur. The effects of the operating parameters, including the concentrations of H2SO4 and MnS2O6 and the temperature, on the conversion rate of MnS2O6 were investigated. The kinetic characteristics of the MnS2O6 conversion were analyzed. The results indicated that MnS2O6 decomposed into MnSO4 and SO2 in the H2SO4-MnO2 system through two pathways. (A) MnS2O6 decomposed into MnSO4 and SO2 in the presence of H2SO4 in the disproportionation reaction, and SO2 was oxidized to MnSO4 by MnO2 in the liquid phase. (B) The direct oxidizing reaction of MnS2O6 with MnO2 resulted in the formation of MnSO4 in H2SO4 solution. The former pathway was predominant in the MnS2O6 conversion. In addition, based on the results of the MnS2O6 conversion in the H2SO4-MnO2 system, the kinetics analysis of the composite reaction was conducted, and the apparent activation energy (Ea) of 204.6 kJ mol(-1) was obtained. (C) 2020 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.
机译:二萜是副产品,伴有锰硫酸盐的形成,含硫二氧化硫(SO2)的浸出过程与热溶胶。通过使MNSO4产物的纯度降低,可以产生的MnS2O6对于回收MNSO4是不利的。为了获得合格的MNSO4产品,从浸出溶液中移除MNS2O6至关重要。在这项工作中,研究了H2SO4-MNO2系统中MNS2O6的转化特性。 MNS2O6的转化机制由硫的材料平衡确定。研究了操作参数的效果,包括H 2 SO 4和MnS2O6的浓度和温度,对MNS2O6的转化率进行了研究。分析了MNS2O6转化率的动力学特征。结果表明,通过两种途径将MNS2O6分解成MnSO4和SO 2。 (a)在歧化反应的H 2 SO 4存在下分解成MnSO4和SO2的MNS2O6,通过MNO 2在液相中通过MNO 4氧化至MNSO 4。 (b)MNS2O6与MnO 2的直接氧化反应导致H 2 SO 4溶液中的MnSO 4形成。在MNS2O6转化中,前途径是主要的。另外,基于H2SO4-MNO2系统中的MNS2O6转化的结果,进行了复合反应的动力学分析,得到了204.6kJ摩尔(-1)的表观活化能量(EA)。 (c)2020日本粉末科技会。由elsevier b.v发表。和日本粉末科技会。版权所有。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号