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首页> 外文期刊>Waste Management >Char and tar formation during hydrothermal gasification of dewatered sewage sludge in subcritical and supercritical water: Influence of reaction parameters and lumped reaction kinetics
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Char and tar formation during hydrothermal gasification of dewatered sewage sludge in subcritical and supercritical water: Influence of reaction parameters and lumped reaction kinetics

机译:亚临界和超临界水中脱水污泥水热气化过程中的焦炭和焦油形成:反应参数和集总反应动力学的影响

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摘要

The hydrothermal gasification of dewatered sewage sludge converts waste into syngas fuel (gas containing H-2, CH4, Co, and CO2), but the formation of char and tar by a side reaction restricts practical applications. In this study, the formation of char/tar by the hydrothermal gasification of dewatered sewage sludge at 300-400 degrees C for 5-90 min with a heating rate of 8-50 degrees C/min is investigated. The results showed that the formation of tar/char reached equilibrium after 30 min, and an increase in the temperature and heating rate reduced the char yield. However, a higher tar yield was achieved at the highest temperature. Experiments on sludge with different moisture contents were also conducted, and the formation of char/tar was inhibited at a higher moisture content. The addition of NaOH and H2O2 can effectively reduce the char and tar yields, respectively. A lumped kinetic model for describing carbon conversion during the hydrothermal gasification of sewage sludge was developed to elucidate the char/tar formation mechanism. The experimental data were used to determine the model parameters, and the fitting results showed that solid-solid conversion from organic matter in sludge was the predominant char/tar formation pathway, with an activation energy of 7.1 kJ/mol. The experiments using the model compounds indicated that humus and protein are the main precursors of char and tar, respectively. This study provides insights for understanding the formation of char/tar from sewage sludge following hydrothermal gasification, which is vital for controlling the formation of char and tar to improve the gasification efficiency. (C) 2019 Elsevier Ltd. All rights reserved.
机译:脱水污泥的水热气化将废物转化为合成气燃料(含有H-2,CH4,Co和CO2的气体),但是副反应形成的焦炭和焦油限制了实际应用。在这项研究中,研究了脱水污水污泥在300-400摄氏度,加热速度8-50摄氏度/分钟的条件下进行水热气化5-90分钟而形成的焦炭/焦油。结果表明,焦油/焦炭的形成在30分钟后达到平衡,并且温度和加热速率的升高降低了焦炭收率。然而,在最高温度下获得了更高的焦油收率。还对不同水分含量的污泥进行了实验,并在较高水分含量下抑制了焦炭/焦油的形成。 NaOH和H2O2的添加可以分别有效地降低炭和焦油的收率。建立了用于描述污水污泥水热气化过程中碳转化的集总动力学模型,以阐明炭/焦油形成机理。实验数据用于确定模型参数,拟合结果表明污泥中有机物的固-固转化是主要的焦炭/焦油形成途径,活化能为7.1 kJ / mol。使用模型化合物进行的实验表明,腐殖质和蛋白质分别是木炭和焦油的主要前体。该研究为理解热液气化后污水污泥中焦炭/焦油的形成提供了见识,这对于控制焦炭和焦油的形成以提高气化效率至关重要。 (C)2019 Elsevier Ltd.保留所有权利。

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