沸石
催化作用
碱金属
吸附
硅酸钠
烧结
热液循环
化学工程
化学
材料科学
无机化学
废物管理
有机化学
冶金
工程类
作者
Yangang Mei,Qian Zhang,Songping Gao,Yanfeng Xue,Zhiqing Wang
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2023-05-14
卷期号:37 (11): 7911-7918
被引量:1
标识
DOI:10.1021/acs.energyfuels.3c01128
摘要
Catalytic gasification ash (CGA) imposes potential hazards to the environment and additional costs for gasification. To recover the alkali catalysts and to reutilize CGA, the deactivation of Na2CO3, zeolite preparation by hydrothermal processing of CGA (HPGA), and the Cu2+ adsorption behaviors of the prepared zeolite and its kinetics were studied. The results show that the catalytic reactivity of Na2CO3 is very high, but Na2CO3 is easy to generate deactivated sodium aluminum silicate (NaAlSiO4). These reactions are responsible for the deactivation of Na2CO3, but fortunately, the process of Na2CO3 deactivation during gasification also can accomplish the activation of Al and Si matters in coal. As a result, CGA can directly transform into zeolite by HPGA without further alkali addition and sintering treatment. Simultaneously, 41% of Na can be recovered during HPGA, and the prepared zeolite has a much higher Cu2+ adsorption capacity compared with CGA. The novel process of catalyst recovery coupled with zeolite preparation provides a feasible and environmentally friendly way for utilization of CGA without alkali addition and sintering treatment.
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