首页> 外文期刊>Archives of Environmental Protection >SIMUlTANEOUS NITRIFICATION AND DENITRIFICATION IN AN SBR WITH A MODIFIED CYClE DURING REJECT WATER TREATMENT
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SIMUlTANEOUS NITRIFICATION AND DENITRIFICATION IN AN SBR WITH A MODIFIED CYClE DURING REJECT WATER TREATMENT

机译:循环水处理后具有改性环的SBR同时进行硝化和反硝化

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In this study, the dependence between volumetric exchange rate (n) in an SBR (Sequencing Batch Reactor) with a modified cycle and simultaneous nitrification and denitrification (SND) efficiency during the treatment of anaerobic sludge digester supernatant was determined. In the SBR cycle alternating three aeration phases (with limited dissolved oxygen (DO) concentration up to 0.7 mg O/l) and two mixing phases were applied. The lengths of each aeration and mixing phases were 4 and 5.5 h, respectively.Independently of n, a total removal of ammonium was achieved. However, at n = 0.1 d~(-1) and n = 0.3 d~(-1) nitrates were the main product of nitrification, while at n = 0.5 d~(-1), both nitrates and nitrites occurred in the effluent. Under these operational conditions, despite low COD/N (ca. 4) ratio in the influent, denitrification in activated sludge was observed. A higher denitrification efficiency at n = 0.5 d~(-1) (51.3%) than at n = 0.1 d~(-1) (7.8%) indicated that n was a crucial factor influencing SND via nitrite and nitrate in the SBR with a low oxygen concentration in aeration phases.
机译:在这项研究中,确定了具有改进周期的SBR(测序间歇反应器)中的体积交换速率(n)与厌氧污泥消化池上清液的同时硝化和反硝化(SND)效率之间的依赖性。在SBR循环中,交替使用三个曝气阶段(溶解氧(DO)的浓度限制为0.7 mg O / l)和两个混合阶段。每个曝气阶段和混合阶段的长度分别为4和5.5 h。独立于n,可以完全去除铵。然而,在n = 0.1 d〜(-1)和n = 0.3 d〜(-1)时,硝酸盐是硝化的主要产物,而在n = 0.5 d〜(-1)时,污水中同时发生硝酸盐和亚硝酸盐。 。在这些操作条件下,尽管进水的COD / N比(约4)低,但仍观察到活性污泥的反硝化作用。 n = 0.5 d〜(-1)(51.3%)时的反硝化效率高于n = 0.1 d〜(-1)(7.8%)时的反硝化效率,表明n是通过SBR中的亚硝酸盐和硝酸盐影响SND的关键因素。曝气阶段氧气浓度低。

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