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通过水力空化预处理提高含油废水与剩余活性污泥连续共消化的沼气产量。

Improving biogas production from continuous co-digestion of oily wastewater and waste-activated sludge by hydrodynamic cavitation pre-treatment.

作者信息

Habashi Nima, Alighardashi Abolghasem, Mennerich Artur, Mehrdadi Nasser, Torabian Ali

机构信息

a Faculty of Environment , University of Tehran , Tehran , Iran.

b Faculty of Civil and Environmental Engineering , Ostfalia University of Applied Sciences , Suderburg , Germany.

出版信息

Environ Technol. 2018 Apr;39(8):1017-1024. doi: 10.1080/09593330.2017.1318181. Epub 2017 Apr 27.

Abstract

Hydrodynamic cavitation (HC) was evaluated as a pretreatment for synthetic oily wastewater (OWW) to be co-digested with waste-activated sludge (WAS). The main objective of the present research was the enhancement of biogas production by the application of HC pretreatment. HC was applied to the OWW, and the OWW and WAS were added to a 50 L continuous digestion reactor. As a control system, an identical digestion reactor was set up for co-digestion of the WAS and the OWW without pretreatment. The reactors were initially filled with inoculum and the hydraulic retention time (HRT) was set to 22 d. The HRT was gradually reduced to 19, 16, and finally 13 d, but the substrate quality was kept constant. The loading rate, accordingly, increased from 0.86 to 1.46 g TVS/(L d). The biogas volume was recorded online and its quality was analyzed regularly. The HC improved biogas production up to 43% at 22 d of HRT. Reducing the HRT decreased biogas production from the main reactor while that of the control reactor was more or less constant. HC also increased the biogas methane content; the methane concentration of the main reactor was about 3% higher than the methane concentration of the control reactor. The main reactor experienced no clogging or accumulation of fatty materials.

摘要

对水力空化(HC)作为合成含油废水(OWW)与废弃活性污泥(WAS)共消化预处理方法进行了评估。本研究的主要目的是通过应用HC预处理提高沼气产量。对OWW进行HC处理,然后将OWW和WAS加入到一个50升的连续消化反应器中。作为对照系统,设置了一个相同的消化反应器用于未经预处理的WAS和OWW的共消化。反应器最初填充接种物,水力停留时间(HRT)设置为22天。HRT逐渐降至19天、16天,最后降至13天,但底物质量保持不变。相应地,负荷率从0.86克挥发性固体/(升·天)增加到1.46克挥发性固体/(升·天)。在线记录沼气产量,并定期分析其质量。在HRT为22天时,HC使沼气产量提高了43%。缩短HRT会降低主反应器的沼气产量,而对照反应器的沼气产量大致保持不变。HC还提高了沼气中的甲烷含量;主反应器的甲烷浓度比对照反应器的甲烷浓度高约3%。主反应器未出现堵塞或脂肪物质积累的情况。

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