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Comparison of different fluid dynamics in activated sludge system for the treatment of a stimulated milk processing wastewater: Process analysis and optimization

机译:活性污泥系统中不同流体动力学处理刺激奶加工废水的比较:过程分析和优化

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摘要

Wastewater from the milk industry usually undergoes activated sludge ahead of refining treatments, final discharge or reuse. To identify the most effective bioreactor hydraulic regime for the secondary treatment of wastewater resulting from the milk industry in an activated sludge system, two lab-scale activated sludge systems characterized by a different configuration and fluid dynamics (i.e., a compartmentalized activated sludge (CAS) with plug flow regime and a complete mixed activated sludge (AS)) were operated in parallel, inoculated with the same microbial consortium and fed with identical streams of a stimulated dairy wastewater. The effect of three process and operational variables-influent chemical oxygen demand (COD) concentration, sludge recycle ratio (R) and hydraulic retention time (HRT)-on the performance of the two systems were investigated. Experiments were conducted based on a central composite face-centered design (CCFD) and analyzed using response surface methodology (RSM). The region of exploration for treatment of the synthetic wastewater was taken as the area enclosed by the COD_(in) (200, 1,000 mg/l), R (1, 5), and HRT (2, 5 h) boundaries. To evaluate the process, three parameters, COD removal efficiency (E), specific substrate utilization rate (U), and sludge volume index (SVI), were measured and calculated over the course of the experiments as the process responses. The change of the flow regime from complete-mix to plug flow resulted in considerable improvements in the COD removal efficiency of milk wastewater and sludge settling properties. SVI levels for CAS system (30-58 ml/g) were considerably smaller that for the AS system (50-145 ml/g). In addition, the biomass production yield could be reduced by about 10% compared to the AS system. The results indicated that for the wastewater, the design HRT of a CAS reactor could be shortened to 2-4 h.
机译:牛奶行业的废水通常在精制处理,最终排放或再利用之前经过活性污泥处理。为了确定活性污泥系统中牛奶工业废水的二级处理最有效的生物反应器水力工况,采用了两个实验室规模的活性污泥系统,它们具有不同的结构和流体动力学特征(即,隔室活性污泥(CAS))并联运行,并使用完全混合的活性污泥(AS)并行操作,接种相同的微生物联合体,并喂入相同的经刺激的乳制品废水流。研究了三个过程和操作变量-进水化学需氧量(COD)浓度,污泥再循环率(R)和水力停留时间(HRT)-对两个系统性能的影响。实验基于中央复合人脸中心设计(CCFD)进行,并使用响应面方法(RSM)进行了分析。以合成废水处理的勘探区域为COD_(in)(200,1,000 mg / l),R(1、5)和HRT(2、5 h)边界所包围的区域。为了评估该过程,在实验过程中测量并计算了三个参数,即COD去除效率(E),特定底物利用率(U)和污泥体积指数(SVI),作为过程响应。从完全混合流到活塞流的流态变化导致牛奶废水的COD去除效率和污泥沉降特性得到了显着改善。 CAS系统的SVI水平(30-58 ml / g)显着小于AS系统的SVI水平(50-145 ml / g)。另外,与AS系统相比,生物质生产的产率可以降低约10%。结果表明,对于废水,CAS反应器的设计HRT可以缩短至2-4 h。

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