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直接冷凝法回收二硫化碳的冷量优化探讨
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作者 周治全 《人造纤维》 2021年第3期27-29,共3页
对粘胶纤维生产中采用直接冷凝法回收二硫化碳过程中各级冷凝器的冷量消耗进行了工艺计算,提出了提高冷量利用效率的方法,有效降低了能源成本。
关键词 二硫化碳回收 冷量 冷凝器 换热量
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Separation and enrichment of elemental sulfur and mercury from hydrometallurgical zinc residue using sodium sulfide 被引量:2
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作者 王子阳 蔡晓兰 +3 位作者 张泽彪 张利波 王仕兴 彭金辉 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2015年第2期640-646,共7页
The separation and enrichment of mercury and the recovery of elemental sulfur from flotation sulfur concentrate in zinc pressure leaching process were carried out by sodium sulfide leaching and carbon dioxide precipit... The separation and enrichment of mercury and the recovery of elemental sulfur from flotation sulfur concentrate in zinc pressure leaching process were carried out by sodium sulfide leaching and carbon dioxide precipitating. The results show that the leaching rate of elemental sulfur is more than 98%, and 98.13% of mercury is enriched in the residue, under the optimized conditions of sodium sulfide concentration 1.5 mol/L, liquid/solid ratio 6:1 and leaching time 30 min at room temperature. In addition, the content of mercury is enriched 5.23 times that in the leaching residue. The elemental sulfur is precipitated from leaching solution under conditions of carbon dioxide flow rate 200 mL/min and blowing time 150 min, while solution is stirred adequately. The recovery efficiency of elemental sulfur reaches 97.67%, and the purity of elemental sulfur is 99.75%, meeting the requirements of industrial first-rate product standard according to the national standard of GB/T 2449-2006 (PRC). 展开更多
关键词 flotation sulfur concentrate sodium sulfide leaching carbon dioxide precipitating mercury enrichment elemental sulfurrecovery
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