Recovery of hazardous metals from spent refinery processing solid catalyst

被引:20
作者
Shen, Wei [1 ]
Li, Tao [1 ]
Chen, Junfeng [1 ]
机构
[1] China Waterborne Transport Res Inst, Beijing 100088, Peoples R China
来源
SEVENTH INTERNATIONAL CONFERENCE ON WASTE MANAGEMENT AND TECHNOLOGY (ICWMT 7) | 2012年 / 16卷
关键词
Spent catalyst; Leaching; Heavy metal; Citric acid; HYDRODESULFURIZATION; ALUMINA; AGENTS;
D O I
10.1016/j.proenv.2012.10.035
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The extraction properties of metallic elements from the spent refinery processing catalyst were examined under citric acid leaching conditions. Different temperatures were tested for the extraction experiments and 80 degrees C was found to be most effective for metal extraction from the spent refinery processing catalyst. Compared to room condition, citric acid leaching treatment with 80 degrees C accelerated the dissolution of the catalyst waste solid, thus promoted the reaction of acid with hazardous metals such as Al, Ni, Mo. Furthermore, the optimum hydrothermal treatment temperature, time and liquid/solid ratio were 80 degrees C, 10 h and 8:1 (ml: g), respectively. (C) 2012 Selection and/or peer-review under responsibility of Basel Convention Coordinating Centre for Asia and the Pacific and National Center of Solid Waste Management, Ministry of Environmental Protection of China.
引用
收藏
页码:253 / 256
页数:4
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