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首页> 外文期刊>Journal of environmental sciences >Hydraulic characteristics of an anaerobic baffled reactor as onsite wastewater treatment system
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Hydraulic characteristics of an anaerobic baffled reactor as onsite wastewater treatment system

机译:厌氧折流板反应器作为现场废水处理系统的水力特性

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摘要

The feasibility of using anaerobic baffled reactor (ABR) as onsite wastewater treatment system was discussed. The ABR consisted of one sedimentation chamber and three up-flow chambers in series was experimented under different peak flow factors (PFF of 1 to 6), superficial gas velocities (between 0.6 and 3.1 cm/hr) and hydraulic retention times (HRT) (24, 36 and 48 hr). Residence time distribution (RTD) analyses were carried out to investigate the hydraulic characteristics of the ABR. It was found that the PFF resulted in hydraulic dead space. The dead space did not exceed 13% at PFF of 1, 2 and 4 while there was 2-fold increase (26%) at PFF of 6. Superficial gas velocities did not result in more (biological) dead space. The mixing pattern of ABR tended to be a completely-mixed reactor when PFF increased. Superficial gas velocities did not affect mixing pattern. The effects of PFF on mixing pattern could be minimized by higher HRT (48 hr). The tank-in-series (TIS) model (N = 4) was suitable to describe the hydraulic behaviour of the studied system. The HRT of 48 hr was able to maintain the mixing pattern under different flow patterns, introducing satisfactory hydraulic efficiency. Chemical oxygen demand (COD) and total suspended solids (TSS) removals under all flow patterns were achieved more than 85% and 90%, respectively. The standard deviation of effluent COD and TSS concentration did not exceed 15 mg/L.
机译:讨论了使用厌氧折流板反应器(ABR)作为现场废水处理系统的可行性。在不同的峰值流量因子(PFF为1至6),表观气速(0.6至3.1 cm / hr之间)和水力停留时间(HRT)下,对由一个沉淀室和三个上流室串联的ABR进行了实验24、36和48小时)。进行停留时间分布(RTD)分析以研究ABR的水力特性。发现PFF导致液压死空间。在PFF为1、2和4时,死区不超过13%,而在PFF为6时,死区增加了2倍(26%)。表观气体速度不会导致更多(生物)死区。当PFF增加时,ABR的混合模式倾向于是完全混合的反应器。表观气体速度不影响混合模式。较高的HRT(48小时)可使PFF对混合模式的影响最小化。串联罐(TIS)模型(N = 4)适合描述所研究系统的液压性能。 48小时的HRT能够在不同的流型下保持混合模式,从而带来令人满意的水力效率。在所有流态下,化学需氧量(COD)和总悬浮固体(TSS)的去除率分别达到85%和90%以上。出水COD和TSS浓度的标准偏差不超过15 mg / L。

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