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Anaerobic Treatment of Yeast Effluent in an Expanded Granular Sludge Bed Reactor

机译:膨胀式颗粒污泥床反应器中酵母菌的厌氧处理

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The purpose of this study was to investigate the use of an anaerobic expanded granular sludge bed (EGSB) reactor, to treat high strength yeast wastewater. The EGSB reactor was seeded with granular sludge from the UASB reactor of a full-scale brewery factory. Experiment was done under operational condition of a total superficial up flow velocity(Vup) of 6mȂ2;h-1, Temperature of 30??, COD concentration of about 20 gȂ2;L-1. Startȁ3;up of a step-wise manner was adopted. The volumetric organic loading (BV.TCOD) was increased progressively by varying flow of the influent, and extent of raising BV.TCOD should be less than 30% at each step. After the start-up period of 79 days, the BV.TCOD of the EGSB reactor reached 15.8 kg COD m-3Ȃ2;d-1, and obtained COD removal efficiency of 69.5%. The specific methanogenic activity of the sludge was about twice higher than that of the seeded sludge. The experimental results indicated that the anaerobic treatment of yeast effluent in an EGSB system appears to be a feasible option.
机译:这项研究的目的是研究使用厌氧膨胀颗粒污泥床(EGSB)反应器来处理高强度酵母废水。 EGSB反应器用来自大型啤酒厂的UASB反应器的颗粒污泥播种。实验是在总表面向上流速(Vup)为6mȂ2; h-1,温度为30℃,COD浓度约为20gȂ2; L-1的操作条件下进行的。启动ȁ3;采用逐步方式。通过改变进水流量,逐渐增加有机物的体积含量(BV.TCOD),并且每步的升高BV.TCOD的程度应小于30%。启动79天后,EGSB反应器的BV.TCOD达到15.8 kg CODm-3Ȃ2; d-1,获得的COD去除率为69.5%。污泥的产甲烷比活性大约是播种污泥的产甲烷活性的两倍。实验结果表明,在EGSB系统中厌氧处理酵母废水似乎是一个可行的选择。

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