首页> 外文期刊>Water Science and Technology >Upgrading of an activated sludge wastewater treatment plant by adding a moving bed biofilm reactor as pre-treatment and ozonation followed by biofiltration for enhanced COD reduction: design and operation experience
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Upgrading of an activated sludge wastewater treatment plant by adding a moving bed biofilm reactor as pre-treatment and ozonation followed by biofiltration for enhanced COD reduction: design and operation experience

机译:通过添加移动床生物膜反应器进行预处理和臭氧化,然后进行生物过滤以提高COD减少量来升级活性污泥废水处理厂的设计和操作经验

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A paper mill producing 500,000 ton of graphic paper annually has an onsite wastewaterntreatment plant that treats 7,240,000m3 of wastewater per year, mechanically first, thennbiologically and at last by ozonation. Increased paper production capacity led to highernCOD load in the mill effluent while production of higher proportions of brighter productsngave worse biodegradability. Therefore the biological capacity of the WWTP needed to benincreased and extra measures were necessary to enhance the efficiency of COD reduction.nThe full scale implementation of one MBBR with a volume of 1,230 m3 was accomplishednin 2000 followed by another MBBR of 2,475 m3 in 2002. An ozonation step with a capacitynof 75 kg O3/h was added in 2004 to meet higher COD reduction demands during thenproduction of brighter products and thus keeping the given outflow limits. Adding a movingnbed biofilm reactor prior to the existing activated sludge step gives: (i) cost advantagesnwhen increasing biological capacity as higher COD volume loads of MBBRs allow smallernreactors than usual for activated sludge plants; (ii) a relief of strain from the activatednsludge step by biological degradation in the MBBR; (iii) equalizing of peaks in the CODnload and toxic effects before affecting the activated sludge step; (iv) a stable volumensludge index below 100 ml/g in combination with an optimization of the activatednsludge step allows good sludge separation—an important condition for further treatmentnwith ozone. Ozonation and subsequent bio-filtration pre-treated waste water provide:n(i) reduction of hard COD unobtainable by conventional treatment; (ii) controllable CODnreduction in a very wide range and therefore elimination of COD-peaks; (iii) reduction ofntreatment costs by combination of ozonation and subsequent bio-filtration; (iv) decreasenof the color in the ozonated wastewater. The MBBR step proved very simple to operatenas part of the biological treatment. Excellent control of the COD-removal rate in thenozone step allowed for economical usage and therefore acceptable operation costs innrelation to the paper production.
机译:一家年产50万吨图形纸的造纸厂拥有一个现场废水处理厂,该厂每年首先通过机械方式,生物技术和最后通过臭氧处理来处理724万立方米的废水。造纸能力的提高导致工厂废水中较高的COD负荷,而更高比例的光亮产品的生产却使生物降解性变差。因此,需要提高污水处理厂的生物能力,并且必须采取额外措施来提高COD的降低效率。n2000年完成了一个容量为1,230 m3的MBBR的全面实施,2002年又完成了2,475 m3的另一个MBBR。 2004年增加了容量为75 kg O3 / h的臭氧化步骤,以满足在生产更光亮产品过程中对COD降低的更高要求,从而保持给定的流出极限。在现有的活性污泥步骤之前添加移动床生物膜反应器可:(i)提高生物容量时的成本优势,因为较高的COBR量的MBBRs负载使反应器比通常的活性污泥装置更小; (ii)通过MBBR中的生物降解减轻活性污泥步骤中的应变; (iii)在影响活性污泥步骤之前,使CODnload的峰值和毒性影响均等; (iv)低于100 ml / g的稳定污泥指数结合优化的活性污泥步骤可实现良好的污泥分离,这是用臭氧进一步处理的重要条件。臭氧化和随后的生物过滤预处理废水提供:n(i)减少常规处理无法获得的硬化学需氧量; (ii)在很宽的范围内可控制地减少CODn,因此消除了COD峰值; (iii)通过臭氧化和随后的生物过滤相结合来降低处理成本; (iv)降低臭氧化废水的颜色。事实证明,MBBR步骤非常易于操作,是生物处理的一部分。在nozone步骤中出色地控制了COD的去除速度,可以经济地使用,因此可以接受与造纸无关的操作成本。

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