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Theoretical and Experimental Investigation of Sewage Sludge Gasification Process in a Fixed Bed Reactor

机译:固定床反应器中污泥气化过程的理论和实验研究

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The paper presents an experimental and theoretical investigation of a sewage sludge gasification process. An experimental installation with an downdraft gasifier was used. Theoretical analysis has been focused on the calculation of the gas composition from sludge gasification using equilibrium modeling. In both cases the influence of composition, volatile matter, water and heavy metal content of the syngas composition of sewage sludge was examined. The results show that greater oxygen content in sewage sludge causes a reduction in the reaction temperature. As expected, increasing the air flow rate caused a decrease in the heating value of the produced gas. A higher amount of oxidizer increases the amounts of noncombustible species and volumetric fraction of nitrogen, thus reducing the heating value of the obtained gas. Higher water content in the sewage sludge affects the gasification gas composition. As a result, combustible components are in the minority in the syngas.
机译:本文介绍了污水污泥气化过程的实验和理论研究。使用了具有下行气流气化炉的实验装置。理论分析一直集中在使用平衡模型从污泥气化中计算气体成分。在这两种情况下,都检查了污水污泥合成气组成的组成,挥发物,水和重金属含量的影响。结果表明,污水污泥中较高的氧含量导致反应温度降低。如所期望的,增加空气流速导致所产生的气体的热值降低。较高量的氧化剂增加了不可燃物质的量和氮的体积分数,因此降低了所获得气体的热值。污水污泥中较高的水含量会影响气化气体的组成。结果,合成气中的可燃成分很少。

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