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High rate anaerobic digestion of primary and secondary sludge using the static granular bed reactor (SGBR)

机译:使用静态颗粒床反应器(SGBR)对初级和次级污泥进行高速厌氧消化

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摘要

The aim of this research was to demonstrate the feasibility of the static granular bed reactor (SGBR) as a replacement for the conventional mixed and heated anaerobic digester typically operating at municipal wastewater treatment plants (WWTP). The static granular bed reactor (SGBR) is a high rate anaerobic granular reactor. The SGBR operates at a short hydraulic retention time (HRT) (i.e 1 to 2 d) while maintaining a long solids retention time (SRT). Conversely to conventional digesters the SGBR separates the SRT from the HRT, reducing energy and volume requirements. The SGBR is downflow reactor with a dense bed of granules that entraps particles which helps to facilitate hydrolysis. Anaerobic treatment of primary and secondary municipal sludge was studied with a laboratory and pilot-scale SGBR at organic loading rates (OLR) from 2.8 ± 0.9 to 5.5 ± 1.7 g COD/L·d and 3.3 ± 2.0 g COD/L·d, respectively. The results of this research demonstrated the SGBR system\u27s potential to be a practical and competitive alternative to conventional anaerobic digestion of wastewater sludges. The laboratory (76 ± 4%) and pilot-scale (71 ± 0.4%) SGBR produced a biogas with a higher methane content than the conventional anaerobic digester tested (59 ± 2.8%). Effluent VFA concentrations remained below 40 mg/L as HAc, indicating the potential to reduce process instability due to the buildup of intermediates. The low VFA concentrations of the SGBR\u27s effluent also reduces odors compared to the liquid streams of conventional anaerobic digesters. The SGBR produced an effluent with low organic matter; average TSS and COD removal efficiencies remained above 90%.
机译:这项研究的目的是证明静态颗粒床反应器(SGBR)替代通常在市政废水处理厂(WWTP)中运行的常规混合和加热厌氧消化池的可行性。静态颗粒床反应器(SGBR)是一种高速厌氧颗粒反应器。 SGBR在较短的水力停留时间(HRT)(即1至2 d)下运行,同时保持较长的固体停留时间(SRT)。与传统的蒸煮器相反,SGBR将SRT与HRT分开,从而减少了能源和体积需求。 SGBR是具有浓密颗粒床的下流反应器,该颗粒床会截留颗粒,这有助于促进水解。使用实验室和中试规模的SGBR在有机负荷率(OLR)为2.8±0.9至5.5±1.7 g COD / L·d和3.3±2.0 g COD / L·d的条件下研究了一级和二级市政污泥的厌氧处理,分别。这项研究的结果表明,SGBR系统具有替代常规厌氧消化污泥的潜力,具有实用性和竞争性。实验室(76±4%)和中试规模(71±0.4%)SGBR生产的沼气比测试的常规厌氧消化池(59±2.8%)的甲烷含量更高。废水中的VFA浓度以HAc的形式保持在40 mg / L以下,这表明有可能减少由于中间体的堆积而引起的工艺不稳定。与常规厌氧消化池的液流相比,SGBR废水的低VFA浓度也减少了气味。 SGBR产生的废水中有机物含量低; TSS和COD的平均去除效率保持在90%以上。

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    Biese, Tyler J.;

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  • 年度 2016
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