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Inhibition of Catalyst Poisoning in Supercritical Water Gasification of Sewage Sludge: Technical Study on Reactor Design

机译:污水污泥超临界水气化中催化剂中毒的抑制:反应器设计技术研究

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A lab-scale batch reactor with two compartments, so called two-bed reactor, was introduced tothe supercritical water gasification of sewage sludge. With Ni catalyst presence, the reactor was capableof suppressing deposition of byproducts and residuals on catalyst surface attaining higher gasificationefficiencies. Moreover, acceleration of hydrogen gas production was achieved when K_2CO_3 was loadedwith the presence of Ni catalyst. Further studies have revealed that K_2CO_3 loading location influencedthe gasification behavior dramatically. Besides Ni catalyst, RuO_2 and Ru catalyst were also employedusing the reactor. In prospect of future application, discussion on heavy metal concentration in theeffluent is made as well.
机译:将具有两个隔室的实验室规模的间歇反应器,即所谓的两床反应器,引入到 污水污泥的超临界水气化。在镍催化剂存在下,反应器能够 抑制气化程度更高的催化剂表面副产物和残留物的沉积 效率。此外,当负载K_2CO_3时,实现了氢气生产的加速。 在镍催化剂的存在下。进一步的研究表明K_2CO_3的加载位置会影响 气化行为显着。除Ni催化剂外,还使用RuO_2和Ru催化剂 使用反应堆。在未来的应用前景中,关于重金属浓度的讨论 也会产生废水。

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