He Sheng-bing, Xue Gang, Wang Bao-zhen
School of Environmental Science and Engineering, Shanghai Jiaotong University, 800 Dongchuan Road, Minhang District, Shanghai 200240, PR China.
J Hazard Mater. 2006 Jul 31;135(1-3):406-11. doi: 10.1016/j.jhazmat.2005.12.002. Epub 2006 Feb 28.
Total experimental period was divided into two stages. At first stage, a series of batch studies were carried out to get an understanding of the effect of ozonation on sludge properties. At the following stages, three membrane bioreactors (MBRs) with different amounts of activated sludge to be ozonated were run in parallel for a long period to evaluate the influence of sludge ozonation on sludge yield and permeate quality. Through batch study, it was found that ozone could disrupt the cell walls and cause the release of plasm from the cells, then the amounts of soluble organics in the solution increased with ozonation time. With the rise of soluble organics, the amount of soluble organics to be mineralized increased as well, which would reduce the soluble organics content. For the counteraction between these two aspects, a pseudo-balance could be achieved, and soluble organics would vary in a limited range. Sludge ozonation also increased the contents of soluble nitrogen and phosphorus in the solution. On the basis of batch study, a suitable ozone dosage of 0.16 kg O(3)/kg MLSS was determined. Three systems were run in parallel for a total period of 120 days; it was demonstrated that a part of activated sludge ozonation could reduce sludge production significantly, and biological performance of mineralization and nitrification would not be inhibited due to sludge ozonation. Experimental results proved that the combination of ozonation unit with MBR unit could achieve an excellent quality of permeate as well as a small quantity of sludge production, and economic analysis indicated that an additional ozonation operating cost for treatment of both wastewater and sludge was only 0.096 Yuan (US$ 0.0115)/m(3) wastewater.
整个实验期分为两个阶段。在第一阶段,进行了一系列批次研究以了解臭氧化对污泥性质的影响。在接下来的阶段,三个含有不同量待臭氧化活性污泥的膜生物反应器(MBR)并行运行了很长一段时间,以评估污泥臭氧化对污泥产量和渗透液质量的影响。通过批次研究发现,臭氧可破坏细胞壁并导致细胞内物质释放,随后溶液中可溶性有机物的量随臭氧化时间增加。随着可溶性有机物的增加,待矿化的可溶性有机物量也增加,这将降低可溶性有机物含量。由于这两个方面的相互作用,可以达到一种准平衡,可溶性有机物将在有限范围内变化。污泥臭氧化还增加了溶液中可溶性氮和磷的含量。基于批次研究,确定了合适的臭氧投加量为0.16 kg O₃/kg MLSS。三个系统并行运行了120天;结果表明,对部分活性污泥进行臭氧化可显著减少污泥产量,且污泥臭氧化不会抑制矿化和硝化的生物学性能。实验结果证明,臭氧化单元与MBR单元相结合可实现优异的渗透液质量以及少量的污泥产量,经济分析表明,处理废水和污泥的额外臭氧化运行成本仅为0.096元(0.0115美元)/m³废水。