首页> 外文期刊>Metallurgical and Materials Transactions B >Separation of Antimony from a Stibnite Concentrate Through a Low-Temperature Smelting Process to Eliminate SO2 Emission
【24h】

Separation of Antimony from a Stibnite Concentrate Through a Low-Temperature Smelting Process to Eliminate SO2 Emission

机译:通过低温熔融工艺从锑矿精矿中分离锑以消除SO 2 排放

获取原文
获取原文并翻译 | 示例
           

摘要

The main purpose of this study is to characterize and separate antimony from a stibnite concentrate through a low-temperature sulfur-fixing smelting process. This article reports on a study conducted on the optimization of process parameters, such as flux and zinc oxide weight percentage, in charging, smelting temperature, smelting duration on the antimony yield, resultant crude antimony grade, and sulfur-fixing rate. A maximum antimony recovery of 97.07 pct, crude antimony grade of 96.45 pct, and 98.61 pct sulfur-fixing rate are obtained when a charge (containing 63.20 wt pct of flux and 21.30 wt pct of stibnite, a flux composition of WtextNaOH /WtextNa 2 textCO3 W_{text{NaOH}} /W_{{{text{Na}}_{ 2} {text{CO}}_{3} }} = 10/147, where W represents weight, and more than 10 pct of the stoichiometric requirement of zinc oxide dosage) is smelted at 1153 K (880 °C) for 120 minutes. This smelting operation is free from atmospheric pollution because zinc oxide is used as the sulfur-fixing agent. The solid residue is subjected to mineral dressing operation to obtain suspension, which is filtered ultimately to produce a cake, representing the solid particles of zinc sulfide. Based on the results of the chemical content analysis of as-resultant zinc sulfide, more than 90 pct zinc sulfide can be recovered, and the recovered zinc sulfide grade can reach 66.70 pct. This material can be sold as zinc sulfide concentrate or roasted to regenerate into zinc oxide.
机译:这项研究的主要目的是通过低温固硫熔炼工艺从锑辉石精矿中鉴定和分离锑。本文报道了一项关于优化工艺参数的研究,该工艺参数包括装料中的助熔剂和氧化锌的重量百分比,熔炼温度,锑产量的熔炼时间,所得粗锑等级和固硫率。当装料(包含63.20 wt%的助熔剂和21.30 wt%的辉辉石,W助熔剂组成的助熔剂时,可获得最大的锑回收率97.07 pct,粗锑等级96.45 pct和固硫率98.61 pct。 / W textNa 2 textCO 3 W_ {text {NaOH}} / W _ {{{text {Na}} __ { 2} {text {CO}} _ {3}}} = 10/147,其中W代表重量,并且在1153 K(880°C)的温度下冶炼120氧化锌的化学计量要求超过10 pct分钟。由于使用氧化锌作为固硫剂,因此该冶炼操作不受大气污染。对固体残余物进行矿物选矿操作以获得悬浮液,将其最终过滤以产生块状物,其代表了硫化锌的固体颗粒。根据所得到的硫化锌的化学含量分析结果,可以回收90%以上的硫化锌,回收的硫化锌等级可以达到66.70 pct。该材料可作为硫化锌精矿出售或焙烧以再生为氧化锌。

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