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Effects of feeding time and organic loading in an anaerobic sequencing batch biofilm reactor (ASBBR) treating diluted whey

机译:厌氧定序分批生物膜反应器(ASBBR)处理稀释乳清中进料时间和有机负荷的影响

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An investigation was carried out on the performance of an anaerobic sequencing batch biofilm reactor (ASBBR) treating diluted cheese whey when submitted to different feed strategies and volumetric organic loads (VOL). Polyurethane foam cubes were used as support for biomass immobilization and stirring was provided by helix impellers. The reactor with a working volume of 3 L treated 2 L of wastewater in 8-h cycles at 500 rpm and 30 ℃. The organic loads applied were 2, 4, 8 and 12 gCODL~(-1) d~(-1), obtained by increasing the feed concentration. Alkalinity was supplemented at a ratio of 50% NaHCO_3/COD. For each organic load applied three feed strategies were tested: (a) batch operation with 8-h cycle; (b) 2-h fed-batch operation followed by 6-h batch; and (c) 4-h fed-batch followed by 4-h batch. The 2-h fed-batch operation followed by 6-h batch presented the best results for the organic loads of 2 and 4 gCODL~(-1) d~(-1), whereas the 4-h fed-batch operation followed by 4-h batch presented results slightly inferior for the same organic loads and the best results at organic loads of 8 and 12 gCOD L~(-1) d~(-1). The concentration of total volatile acids varied with fill time. For the higher fill times maximum concentrations were obtained at the end of the cycle. Moreover, no significant difference was detected in the maximum concentration of total volatile acids for any of the investigated conditions. However, the maximum values of propionic acid tended to decrease with increasing fill time considering the same organic load. Microbiological analyses revealed the presence of Methanosaeta-like structures and methanogenic hydrogenotrophic-like fluorescent bacilli. No Methanosarcina-like structures were observed in the samples.
机译:厌氧测序批处理生物膜反应器(ASBBR)的性能进行了研究,该反应器适用于不同的进料策略和体积有机负荷(VOL)时处理稀释的干酪乳清。聚氨酯泡沫立方体被用作固定生物质的载体,并且由螺旋叶轮提供搅拌。工作容积为3 L的反应器在500 rpm和30℃的8小时循环中处理了2 L废水。通过增加进料浓度获得的有机负荷为2、4、8和12 gCODL _(-1)d〜(-1)。以50%NaHCO_3 / COD的比例补充碱度。对于每种施加的有机负荷,测试了三种进料策略:(a)8小时循环的分批操作; (b)2小时补料分批操作,然后进行6小时分批; (c)4小时补料,然后进行4小时补料。对于2 g和4 gCODL〜(-1)d〜(-1)的有机负荷,2 h补料分批操作呈现最佳结果,而4 h补料分批操作随后在相同有机负荷下,4 h批次的结果略逊一筹,在有机负荷为8和12 gCOD L〜(-1)d〜(-1)时,最佳结果最佳。总挥发性酸的浓度随填充时间而变化。对于较高的填充时间,在循环结束时获得最大浓度。此外,对于任何研究条件,总挥发性酸的最大浓度均未检测到显着差异。然而,考虑到相同的有机负荷,丙酸的最大值倾向于随着填充时间的增加而降低。微生物学分析显示,存在甲烷菌样结构和产甲烷氢营养型荧光杆菌。样品中未观察到甲烷藻样结构。

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