首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Study of a compact bioreactor for the in-line treatment of dairy wastewaters:case of effluents produced on breeding farms
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Study of a compact bioreactor for the in-line treatment of dairy wastewaters:case of effluents produced on breeding farms

机译:用于奶牛废水在线处理的紧凑型生物反应器的研究:以养殖场产生的废水为例

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A new bioreactor structure is proposed for the in-line biological treatment of the effluents from dairy breeding farms.These wastewaters,called White Waters,are produced twice a day when the milking unit is cleaned.To be suitable in this context,the water treatment process has to satisfy efficiency,technological and cost criteria.The reactor designed operates as a Sequential Batch Reactor in which the settlement phase is replaced by a filtration step.A two-phase flow nozzle(hydro-ejector)is used both to aerate the mixed liquid sludge and to improve the filtration performance.The study of the process was carried out in three steps:(i)analysis of the transfer potential in tap water and with a baker's yeast suspension,(ii)analysis of the treatment performance using simulated dairy wastewater,(iii)treatment of real White Waters produced on a farm.The influence of the operating conditions(mainly permeate flow rate,and liquid and air flow rates in the membrane)on membrane fouling were examined in the aim of increasing the time between membrane regeneration steps.Although the real White Waters presented variations in their characteristics,this principle allowed their efficient treatment in a single step(total retention of the suspended solids,mean COD value of the permeate lower than 125 mg.L~(-1))without the need for an initial mixing tank or for any post-treatment process.
机译:提出了一种新的生物反应器结构,用于对奶牛养殖场的废水进行在线生物处理。当清洗挤奶装置时,每天两次产生这些废水,称为白水。为适应这种情况,水处理工艺必须满足效率,技术和成本标准。设计的反应器按顺序分批反应器运行,其中沉降阶段由过滤步骤代替。两相流喷嘴(加氢喷射器)均用于对混合气充气该过程的研究分三个步骤进行:(i)分析自来水和面包酵母悬浮液中的转移潜力,(ii)使用模拟乳制品分析处理性能废水,(iii)处理农场生产的真实白水。研究了操作条件(主要是渗透液流速,膜中的液体和空气流速)对膜污染的影响为了增加膜再生步骤之间的时间,尽管实际的白水特性有所不同,但该原理允许它们在一个步骤中进行有效处理(悬浮固体的总保留量,渗透物的平均COD值低于125 mg.L〜(-1)),而无需初始混合罐或任何后处理工艺。

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