文章摘要
加压浸出法从失效重整催化剂中分离铂铼
Separation of Pt and Re from spent reforming catalysts by pressure leaching
投稿时间:2020-10-12  
DOI:
中文关键词: 有色金属冶金  失效催化剂      回收  分离
英文关键词: non-ferrous metallurgy  spent catalyst  platinum  rhenium  recovery  separation
基金项目:云南省科技人才和平台计划项目(2018HB112);云南省重大科技专项(2018ZE001);固废资源化专项(2019YFC1907505)
作者单位
李勇 贵研资源易门有限公司云南 玉溪 651100 
吴喜龙 贵研资源易门有限公司云南 玉溪 651100 
赵雨 贵研资源易门有限公司云南 玉溪 651100 
姚禹 贵研资源易门有限公司云南 玉溪 651100 
鲁俊余 贵研资源易门有限公司云南 玉溪 651100 
张天环 贵研资源易门有限公司云南 玉溪 651100 
连汝德 贵研资源易门有限公司云南 玉溪 651100 
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中文摘要:
      失效铂铼催化剂中铂铼性质相似,难以分离,采用碳酸钠加压浸出选择性分离铼,研究了浸出条件对铼浸出效率的影响。在反应温度为160℃,反应时间为150 min,浸出剂碳酸钠用量为物料量的8%,搅拌速率为500 r/min,液固比为4:1,反应压力为0.5 MPa的条件下,铼浸出率98.5%,铂基本不溶解而留在渣中,实现铂和铼的初步分离。
英文摘要:
      The properties of platinum and rhenium in spent platinum-rhenium catalysts are similar and they are difficult to separate. Sodium carbonate pressure leaching was used to selectively separate rhenium from spent catalysts. The influence of leaching conditions on the leaching efficiency of rhenium was studied. When the leaching conditions were as follows: 160℃ of reaction temperature, 150 mins of reaction time, 8% leaching agent amount of the material, 500 r/min of stirring speed, 4:1 of liquid-solid ratio, and 0.5 MPa of reaction pressure, the leaching rate of rhenium was 98.5%, and the platinum was almost insoluble and remained in the slag, thus realizing the separation of platinum and rhenium.
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