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Polyhydroxyalkanoate Production from Sequencing Batch Reactor System Treating Domestic Wastewater Mixed with Glycerol Waste

机译:从序列批量反应器系统处理与甘油垃圾混合的批量反应器系统的聚羟基烷烃生产

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The study aimed to determine the polyhydroxyalkanoate (PHA) production and treatment efficiency of sequencing batch reactor (SBR) system treating synthetic domestic wastewater (DW) and synthetic domestic wastewater mixed with glycerol waste (DW+GW). The system with a total sequence of 24 h consisted of filling phase (20 min), reaction phase (22 h), settling phase (1 h), and withdrawal phase (40 min). The two-step SBR operation comprised anoxic/aerobic steps of 4/18 h was employed at reaction phase. The system fed with DW+GW produced higher PHA than the system fed with DW. In addition, PHA accumulation in activated sludge obtained from the anoxic step was higher than the aerobic step in which the highest PHA concentration and PHA yield at 1,086.87 mg/L and 61.42% as dry sludge weight, respectively, were attained. The results of treatment efficiency revealed that the anoxic step performed higher removal efficiencies of total kjeldahl nitrogen and total phosphate than the aerobic step, while an opposite result of COD removal efficiency was found.
机译:该研究旨在确定测序批量反应器(SBR)系统的多羟基烷酸酯(PHA)生产和治疗效率处理合成型国内废水(DW)和合成的国内废水与甘油废物(DW + GW)。具有24小时的总序列的系统由填充相(20分钟),反应相(22小时),沉降相(1小时)和戒断相(40分钟)组成。在反应相时,使用两步SBR术中包含4/18小时的缺氧/有氧步骤。通过DW + GW馈送的系统比使用DW的系统产生更高的PHA。另外,从缺氧步骤获得的活性污泥中的PHA积聚高于其在1,086.87mg / L和61.42%的最高PHA浓度和PHA产率的有氧步骤,分别为干污泥重量。治疗效率的结果表明,缺氧步骤的总kjeldaHl氮和总磷酸的除去效率高于好氧步骤,而发现COD去除效率的相反结果。

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