Lysozyme reaction was developed as a novel technique for minimizing the amount of excess sludge in the sequential batch reactor(SBR).In the present work,excess sludge taken from a SBR system was treated by lysozyme reaction and then returned to the reactor.The quality of the effluent water and characteristics of the activated sludge in the SBR were analyzed to determine the effectiveness of the reduction process.The results show that excess sludge production could be reduced to almost 100%in the first30 d of operation and could be reduced to further by 40%in the succeeding 20 d or so.In these time periods,the average removal efficiencies of the chemical oxygen demand and total nitrogen are 87.38%and 52.78%,respectively,whereas the average total phosphorous in the effluent is nearly 17.18%greater than that of the effluent of the reference system.After 50 d of operation,the sludge floc size is in the range of 20 to 80μm,which was smaller than the size prior to the start of the hydrolysis and the ratio of mixed liquor volatile suspended solids/mixed liquor suspended solids increases from 86%to 90%.
以城市污水处理厂污泥为原料,采用磷酸活化-微波热解法制备得到污泥活性炭,并将其用于吸附水溶液中的Cr(VI)。分别采用元素分析仪(Vario EL cube)、比表面积孔径分布测定仪(ASAP2020)、扫描电镜(SEM)和傅里叶红外光谱(FT-IR)等仪器对原污泥及污泥活性炭的表面组成和结构进行表征,探讨污泥活性炭的孔隙结构参数和表面化学性能。通过静态吸附实验,考察了溶液初始pH,接触时间,初始Cr(VI)浓度对污泥活性炭吸附Cr(VI)效果的影响,并探讨了污泥活性炭去除Cr(VI)的机理。实验结果表明,pH越低吸附效果越好,吸附平衡时间为100 h。不同温度下吸附过程均符合Langmuir等温吸附模型,30℃时最大吸附容量为27.55 mg/g;吸附动力学过程符合准二级速率方程(R2>0.99);污泥活性炭对Cr(VI)的去除是一个吸附-还原耦合的过程。
