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Sludge deterioration in a full scale UASB reactor after a pH drop working under low loading conditions

机译:在低负荷条件下pH下降后,全尺寸UASB反应器中的污泥变质

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A full scale UASB reactor treating the effluent of a malting plant was operated during nearly two years. During 37 weeks of operation the reactor worked with a COD removal efficiency of 80% and a biogas production of nearly 300 m(3)/d with a methane content of 77%. After the start up and during these months of operation the volumetric organic load was 4 kgCOD/m(3).d and the specific organic load was between 0.2-0.4 kgCOD/kgVSS.d. The sludge SMA in this period was around 0.25 kgCOD/kg VSS.d. On week 37 as a result of a problem at the industrial process the pH in the reactor dropped to a value of 4.8. After pH recovering, the reactor worked with fluctuating COD values in the exit and showed a downward trend in the COD removal efficiency. On week 81 the presence of filaments in the granules was detected. High proportion of Chloroflexi filaments were detected by FISH in the sludge. Changes in the microbial population caused by the low pH probably destabilize the reactor performance. The presence of filamentous granules in the sludge and its further growing could be encouraged by the pH drop and the low specific organic load applied to the reactor. The low specific organic load was a consequence of the high VSS content in the UASB reactor, due to the lack of purges. The length of the filaments attached to the granules grew throughout time. In order to eliminate the sludge with poor settlement properties a recycle was applied to the reactor. As a consequence, low amount of granular sludge stayed in the reactor. At the end, COD concentration in the influent reached higher values than in normal operation; at the same time a complete sludge wash out occurred. On the other hand, using the same sludge (after the recycle implementation) in a bench scale reactor the good properties of the sludge were completely recovered.
机译:在将近两年的时间内,运行了处理制麦厂废水的全尺寸UASB反应器。在运行的37周中,反应器的COD去除效率为80%,沼气产量接近300 m(3)/ d,甲烷含量为77%。在启动后和运行的这几个月中,有机负荷量为4 kgCOD / m(3).d,比有机负荷为0.2-0.4 kgCOD / kgVSS.d。在此期间,污泥SMA约为0.25 kgCOD / kgVSS.d。在第37周,由于工业过程中的问题,反应器中的pH降至4.8。 pH恢复后,反应器在出口处的COD值波动,并且COD去除效率呈下降趋势。在第81周,检测到颗粒中存在细丝。污泥中的FISH检测到高比例的挠性挠丝。低pH值引起的微生物种群变化可能会破坏反应器的性能。 pH下降和施加到反应器中的低比有机负荷可能会促进污泥中丝状颗粒的存在及其进一步生长。低比有机负荷是由于缺乏吹扫而导致UASB反应器中VSS含量高的结果。附着在颗粒上的细丝的长度随时间增长。为了消除沉降性能差的污泥,将循环应用于反应器。结果,少量的颗粒污泥留在反应器中。最后,进水中的COD浓度达到了比正常操作更高的值;同时发生了彻底的污泥冲刷。另一方面,在台式规模的反应器中使用相同的污泥(在循环实施之后),污泥的良好特性得以完全恢复。

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