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Enhanced hydrogen production in co-gasification of sewage sludge and industrial wastewater sludge by a pilot-scale fluidized bed gasifier

机译:通过先导流化床气化器增强污泥污泥和工业废水污泥的协同气化中的氢气生产

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This research provides a perspective on sludge-to-energy using sewage sludge (SS) and industrial wastewater sludge (IS) co-gasification in a pilot-scale fluidized bed gasifier with temperature controlled at (600-800 degrees C) using IS addition ratio (0%-60%), and steam-tobiomass ratio (S/B) (0-1.0). The experimental results show that the increase in thermal reaction activity occurred in concordance with the increase in the IS addition. The explanation for such phenomena is that relatively high catalytic Fe/Mn content in industrial wastewater sludge could lower the activation energy. Hydrogen production was increased from 9.1% to 11.94% with an increase in industrial wastewater sludge ratios from 0% to 60%. The produced gas heating value ranged from 4.84 MJ/Nm(3) to 5.11 MJ/Nm(3), which was coupled with the cold gas efficiency (CGE) ranging from 33.91% to 36.15%. Enhanced hydrogen production in sewage sludge and industrial wastewater sludge co-gasification is investigated in this study. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:本研究提供了使用污水污泥(SS)和工业废水污泥(IS)在先导式流化床气化器中的工业废水污泥(IS)在(600-800℃)中使用的添加比率进行污泥 - 能量污泥(IS)的视角(0%-60%)和蒸汽 - 致染​​色比(S / B)(0-1.0)。实验结果表明,随着添加的增加,热反应活性的增加是一致的。这种现象的解释是工业废水污泥中相对高的催化Fe / Mn含量可以降低激活能量。氢气产量从9.1%增加到11.94%,随着0%至60%的工业废水污泥比率增加。所产生的气体加热值范围为4.84mJ / nm(3)至5.11mm / nm(3),其与冷气效率(CGE)相连,范围为33.91%至36.15%。该研究研究了污水污泥和工业废水污泥协同气化中增强的氢气产量。 (c)2020氢能量出版物LLC。 elsevier有限公司出版。保留所有权利。

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