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首页> 外文期刊>Journal of Cleaner Production >Development of a horizontal reactor with radial agitation to synthesize bio-methane from biomass waste and domestic sewage sludge
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Development of a horizontal reactor with radial agitation to synthesize bio-methane from biomass waste and domestic sewage sludge

机译:用径向搅拌开发水平反应器,从生物质废物和生活污水污泥合成生物甲烷

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Aiming to produce clean energy from biomass, we devised an anaerobic horizontal reactor for the production of biomethane from an innovative combination of agricultural and livestock residues with domestic sewage sludge. Differently from conventional reactors, the horizontal reactor was designed with a radial agitator with finned rectangular blades and a gas chamber to ease CH4 capture. Moisture content in biomass was nearly 90% in acclimation and co-digestion processes. In addition, the pH varied as the substrate was added from 8.5 to 7.55 (fruit and vegetable residue pH was 4.80) and during the digestion process the pH dropped to 5.70 by a Hydraulic Retention Time of 30 days. The reaction system had alkalinized without the use of chemicals, at a pH of 7.60 by the end of the experiment. The acclimated inoculum was processed for a period of 120 days, and produced 254.35 NL of biogas in the anaerobic horizontal reactor. Moreover, the reactor produced 965.55 NL of biogas with the mixture of Acclimated Inoculum, Solid Organic Residue and Domestic Sewage Sludge. The maximum methane concentration of 86% was observed after 73 days, whilst the final methane content was 82% (after 120 days). The reaction process resulted in a biogas production of 0.47 Nm(3)/kgVS and 0.39 Nm(3)CH(4)/kgVS (normalized cubic meters of methane per kilogram of volatile solids). In addition, the net biogas production of the horizontal reactor was 711.20 NL with a rate of 27.59 (NL/day). Finally, a reduction in H2S concentration was observed after the methane concentration had reached about 65%. (C) 2020 Elsevier Ltd. All rights reserved.
机译:旨在从生物量产生清洁能源,我们设计了一种厌氧水平反应器,从农业和家畜残留物与国内污水污泥的创新组合生产生物甲烷。与传统的反应器不同,水平反应器设计有具有翅片矩形叶片的径向搅拌器和气室以易于抑制CH4捕获。生物量的水分含量在适应和共消化过程中接近90%。另外,从8.5-7.55(水果和蔬菜残留物pH为4.80)中加入底物的pH变化,在消化过程中,pH通过30天的液压保留时间降至5.70。在实验结束时,反应系统在没有使用化学物质的情况下碱化,在7.60的pH值下。将所平移的接种物加工为120天,并在厌氧水平反应器中产生254.35 nL的沼气。此外,反应器用适应的接种物,固体有机残留物和国内污水污泥的混合物生产了965.55ng的沼气。在73天后观察到最大甲烷浓度为86%,而最终的甲烷含量为82%(120天后)。反应过程导致沼气产量为0.47nm(3)/ kgvs和0.39nm(3)Ch(4)/ kgvs(每千克挥发性固体的甲烷正常化的立方米)。此外,水平反应器的净沼气产量为711.20ng,速率为27.59(nl /天)。最后,在甲烷浓度达到约65%后观察到H 2 S浓度的降低。 (c)2020 elestvier有限公司保留所有权利。

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