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A combined anaerobic digestion system for energetic brewery spent grain application in co-digestion with a sewage sludge

机译:污水污泥共消化中的能量酿酒厂籽粒应用组合的厌氧消化系统

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In the present study, a combined technology for energetic brewery spent grain (BSG) use in co-digestion with sewage sludge (SS) was presented. A holistic approach that includes the impact of co-substrates and their carriers on the anaerobic digestion (AD) process, and the energetic aspects, was involved. Prior to AD, BSG was pretreated involving the hydrodynamic cavitation (HC); two different carriers were applied: MPW (municipal pre-settled wastewater) and mature landfill leachate (MLL). An orifice plate with a conical concentric hole of 3/10 mm (inlet/outlet diameter) was applied as cavitation device. The initial pressure was 7 bar and the number of recirculation passes through the cavitation zone was 30. The AD experiments were performed in semi-flow reactors, under mesophilic conditions at HRT of 20 and 21 d. In both co-digestion series, the constant co-substrate dose of 6% v/v was adopted. In the presence of cavitated BSG and MPW, a significant increase in biogas/methane production was provided as compared to SS mono-digestion, with the related improvement in kinetic constant by 3.5%. The average biogas yield was 0.48 ± 0.03 m~3 kg~(-1) VS added, while in the control run 0.41 ± 0.03 m~3 kg~(-1) VS added. Using cavitated BSG and MLL, such a beneficial effect was not observed. In both co-digestion series, slightly lower VS removal (as for the control) and stable process performance occurred. Moreover, the improved energy balance was provided. Due to the technological aspects, only co-digestion of cavitated BSG and MPW with SS is recommended for implementation into a full-scale.
机译:在本研究中,提出了一种在与污水污泥(SS)共消化的共同消化中的能量酿酒厂的组合技术。涉及包括共衬底和它们的载体对厌氧消化(AD)过程和能量方面的影响的整体方法。在AD之前,BSG预处理涉及流体动力空化(HC);应用了两种不同的载体:MPW(市前沉淀废水)和成熟垃圾填埋场渗滤液(MLL)。孔板具有3/10mm(入口/出口直径)的锥形同心孔被施加为空化装置。初始压力为7巴,再循环次数通过空化区为30.在半流动反应器中,在20和21d的HRT的中抚化条件下在半流动反应器中进行AD实验。在两个共消化系列中,采用6%v / v的恒定共衬底剂量。在存在有化的BSG和MPW的情况下,与SS单消解相比,提供了沼气/甲烷产生的显着增加,其中动力学恒定的相关改善量为3.5%。添加的平均沼气产量为0.48±0.03m〜3千克〜(-1)Vs,而在控制中,加入0.41±0.03 m〜3 kg〜(-1)Vs。使用空化BSG和MLL,未观察到这种有益效果。在两个共消化系列中,略低于VS去除(如对照),并且发生稳定的工艺性能。此外,提供了改进的能量平衡。由于技术方面,建议仅为全规模实施空气化的BSG和SS具有SS的共消化。

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