The present invention provides a reactor and process for the biological treatment of sewage, being transferred, by gravitational forces with a substantially constant flow rate (Q), through an array of successively alternating aerobic and anaerobic compartments (14, 16) for, respectively, aerobic and anaerobic degradation of biodegradable substances in said sewage, the compartments, which form part of the reactor of the invention, are separated by partition walls (50) and each has a top area (S), the passage of the sewage from an aerobic compartment (16) to its adjacent succeeding anaerobic compartment (14) is provided at the bottom of their common partition wall, while the transfer of sewage from an anaerobic compartment to its adjacent aerobic compartment is performed by means of gravity-caused flow over their common partition wall, whereby oxygen required for the aerobic treatment is dissolved into the sewage via an air-sewage interface at the top area of the anaerobic and aerobic compartments forming thereby a dissolution layer, the depth of oxygen dissolution and, consequently, the oxygen concentration in the dissolution layer at the top area of the compartments being defined by the vertical velocity of the liquid within the compartments, calculates as V=Q/S.
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机译:本发明提供了一种用于污水生物处理的反应器和方法,该污水通过重力以基本恒定的流量(Q)转移,分别通过一系列交替交替的需氧和厌氧隔室(14、16),分别用于所述污水中可生物降解物质的好氧和厌氧降解,形成本发明反应器一部分的隔室由隔壁(50)隔开,并且每个隔室具有顶部区域(S),污水从好氧中通过在其公共分隔壁的底部设有到其相邻的后续厌氧室(14)的隔室(16),而污水通过其公共区域上的重力流从厌氧室转移到其相邻的需氧室。隔墙,好氧处理所需的氧气通过厌氧和好氧合作社顶部区域的空气-污水界面溶解到污水中从而形成溶解层的部分,氧的溶解深度以及因此,在隔室顶部区域的溶解层中的氧浓度由隔室内液体的垂直速度定义,计算为V = Q / S 。
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