混合液悬浮物
流出物
活性污泥
缺氧水域
曝气
化学
制浆造纸工业
挥发性悬浮物
还原电位
总悬浮物
化学需氧量
氮气
污泥膨胀
悬浮物
废物管理
环境工程
环境科学
污水处理
环境化学
废水
无机化学
工程类
有机化学
作者
Zhen Zhou,Qiao Wei-min,Can Xing,Yingjun Wang,Yan Wang,Yifang Wang,Yiru Wang,Luochun Wang
摘要
A modified sludge process reduction activated sludge (SPRAS) technology was developed by inserting a sludge process reduction (SPR) module, composed of an aeration tank and a settler, before the activated sludge system was proposed in this study. Compared with the anaerobic/anoxic/aerobic (AAO) process, the SPRAS resulted in a remarkable decrease in sludge production by 76.6%; sludge decay owing to lengthy solids retention time (about 121.5 d) could be the major cause. During the 217-day operation, the oxidation-reduction potential (ORP) (from 54 to -198 mV) and pH (from 7.8 to 5.0) at the bottom of the SPR settler gradually decreased, and low ORP and pH were in favor of sludge reduction in the SPRAS system. The insertion of the SPR module improved the removal efficiencies of suspended solids, chemical oxygen demand and ammonium nitrogen, and total nitrogen concentration in the effluent was reduced from 23.89 ± 4.82 to 14.16 ± 3.98 mg/L by 50% influent bypassing the SPR module. These results indicated that the SPRAS process could produce much less excess sludge and guarantee better effluent quality than the AAO process.
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