首页> 外文期刊>Journal of Cleaner Production >Minimization of excess bio-sludge and pollution load in oxic-settling-anaerobic modified activated sludge treatment for tannery wastewater
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Minimization of excess bio-sludge and pollution load in oxic-settling-anaerobic modified activated sludge treatment for tannery wastewater

机译:制革废水中的氧沉降-厌氧改性活性污泥处理中的过量生物污泥和污染负荷最小化

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The operational capability of anoxic and anaerobic upgradations to the conventional activated sludge process was tested. A mainstream oxic-settling-anaerobic configuration coupled to the conventional aerobic activated sludge was demonstrated the first time to elucidate the mechanism of excess sludge disruption and pollution removal from real tannery wastewater feed. The given oxic-settling-anaerobic coupled conventional activated sludge configuration, on the lab scale, was operated in parallel with an anoxic modified conventional activated sludge, and an identical conventional activated sludge reactor. The operational performance with emphasis to sludge yield minimization achieved that corresponds to operational strategies followed for the tested process configurations was compared. The oxic-settling-anaerobic coupled conventional activated sludge configuration confirmed around 51% of bio-sludge reduction, and prominent treated effluent quality compared with parallel run conventional activated sludge, and 21% less volatile accumulation than anoxic modified conventional activated sludge system. Furthermore, oxic-settling-anaerobic coupled conventional activated sludge implementation yields a lucrative reduction of feed pollutants including more than 90% removal of soluble and total chemical oxygen demand, total organic carbon, and ammonia nitrogen. Moreover, oxic-settling-anaerobic coupled conventional activated sludge configuration evidenced outstanding operational sustainability toward feed shock loading of tannery influent. The anoxic modified conventional system, on the contrary, witnessed a comparable removal of total chemical oxygen demand (89.8%), and ammonia nitrogen (91.7%). The present study evidenced the key influence of sludge interchange borne hydrolysis-acidification, energy uncoupling, and maintenance metabolism that further supported by batch anaerobic and aerobic digestion of nitrate, phosphate, sulfate, alkalinity, volatile fatty acids, and sludge pool present in the mixed liquid. Importantly, the experimental sludge yield recorded were processed to perform the simulation, and also modification of the sludge retention time correlation reported in the literature. (C) 2019 Elsevier Ltd. All rights reserved.
机译:测试了将缺氧和厌氧升级为常规活性污泥工艺的操作能力。主流的有氧沉降-厌氧结构与传统的好氧活性污泥相结合,首次证明了制革厂废水中过量污泥的破坏和去除污染物的机理。在实验室规模上,给定的氧沉降-厌氧耦合的常规活性污泥配置与缺氧改性的常规活性污泥和相同的常规活性污泥反应器并联运行。比较了以污泥产量最小化为目标的运行性能,该运行性能与测试工艺配置所遵循的运行策略相对应。与平行运行的常规活性污泥相比,氧沉降-厌氧耦合的常规活性污泥构型可减少约51%的生物污泥,并具有显着的处理后污水质量,挥发性积累比无氧改性的常规活性污泥系统少21%。此外,通过氧沉降-厌氧耦合的常规活性污泥的实施,可实现饲料污染物的有利可图的减少,包括去除了90%以上的可溶性和总化学需氧量,总有机碳和氨氮。此外,氧沉降-厌氧耦合的常规活性污泥构型在制革厂进水的进料冲击负荷方面具有出色的运行可持续性。相反,缺氧改良的常规系统的总化学需氧量(89.8%)和氨氮(91.7%)的去除率相当。本研究证明了污泥交换所产生的关键影响是水解-酸化,能量解偶联和维持代谢,这进一步得到混合存在的硝酸盐,磷酸盐,硫酸盐,碱度,挥发性脂肪酸和污泥池的分批厌氧和好氧消化的支持。液体。重要的是,对记录的实验污泥产率进行处理以进行模拟,并修改文献中报道的污泥保留时间相关性。 (C)2019 Elsevier Ltd.保留所有权利。

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