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Anaerobically with biological system growth biofilm bed expanded sumerso

机译:与生物系统厌氧生长的生物膜床扩展苏摩

摘要

The system claimed is based on a process of growing biomass in film created on a submerged expanded backing with bed expanded by downward flow. The flow rate necessary for said expansion is obtained at the expense of the nominal flow rate of effluent, to which is added the elevated rate of recirculation. This elevated rate of recirculation is induced by injection of biogas, which translates into high energy efficiency, inasmuch as both the recirculation and the expansion of the backing bed for the biofilm are obtained by the biogas itself. Said mechanism of injection of biogas will create a liquid column of lesser density, which is the determining factor in the hydraulic head difference capable of creating said flow rate. The process takes placed in a biological reactor, figure 1, comprised of chambers 1, 2, 3 and 4, where the submerged filling 1A, 2A, 3A and 4A of backing pieces for the biofilm is retained. The chambers are connected to form a vertical series. The effluent being treated crosses the various chambers of the reactor in descending flow and its total flow rate of the circulating flow rate and an elevated recirculation rate produces an expansion in the filling, generating a random movement in its elements which favours contact with the biofilm and facilitates the continual removal of the excess biological sludge building up in the sludge concentrator 5. The entire process occurs without contact with the oxygen of air and the recirculation of the effluent realised from the lower end 6 of the reactor to its upper end 7, is achieved by a system of two liquid columns of different density 8, utilising the actual biogas generated in the installation. Not requiring any submerged moving part or equipment - an indisputable advantage of this system - it has elevated energy efficiency, as well as an elevated efficiency for an expanded-bed growth system, enabling an elevated hydraulic head. IMAGE
机译:所要求保护的系统基于使生物质在膜中生长的过程,该膜是在淹没的膨胀背衬上形成的,而床层则通过向下流动而膨胀。所述膨胀所需的流速是以流出物的标称流速为代价而获得的,其中增加了再循环率。循环速度的提高是由注入沼气引起的,转化为高能效,因为沼气本身既可以实现生物膜的再循环又可以扩展生物膜的背衬床。所述注入沼气的机制将产生密度较小的液柱,这是能够产生所述流速的水头差的决定因素。该过程置于图1所示的生物反应器中,该反应器由1、2、3和4室组成,其中保留了用于生物膜的衬底的浸没填充物1A,2A,3A和4A。这些腔室被连接以形成垂直系列。被处理的废水以递减的方式穿过反应器的各个腔室,其总循环流量和循环流量以及升高的再循环速率使填充物膨胀,在其元件中产生随机运动,有利于与生物膜和生物膜的接触。有利于连续去除积聚在污泥浓缩器5中的过量生物污泥。整个过程在不与空气氧气接触的情况下进行,并且使从反应器下端6到其上端7的流出物再循环。通过使用两个密度不同的液柱8的系统来实现,利用系统中产生的实际沼气。不需要任何浸入水中的移动部件或设备-该系统无可争议的优势-它具有提高的能源效率,以及用于扩展床生长系统的更高效率,从而可以提高液压头。 <图像>

著录项

  • 公开/公告号PT102059B

    专利类型

  • 公开/公告日1999-11-30

    原文格式PDF

  • 申请/专利权人 DAVID JORGE PERDIGAO ANTUNES;

    申请/专利号PT19970102059

  • 发明设计人

    申请日1997-10-08

  • 分类号C02F3/28;

  • 国家 PT

  • 入库时间 2022-08-22 01:55:14

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