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The pilot study of enhanced processing against coking wastewater for nitrogen removal in a direct-pass way

机译:强化处理焦化废水直接除氮的中试研究

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From the submerged anaerobic and anoxic pools which have cellular structured fibers fillings for their cross-section,the outbound gas was collected to be re-blown back into the same pool.The aerobic reactor was a Membrane Bio-Reactor(MBR)taking an airlift loop,the activated sludge concentration reached as high as 10-12 g-L-1.During the pilot experiment.an AOA process against coldng wastewater was developed in a direct-pass way.The effluent from the first anaerobic phase was diverged which 10%would not go through the aerobic phase and would go to the third staged pool as a supplemental carbon source.for denitrification.The experiment showed that for influent averaged 2450 mgL-1 CODcr and 95 mgL-1 NH4+-N,the system got a stable effluent of 124 mgL-1 CODcr and 9.8 mg.L-1 NH4+-N.Compared with these ongoing large-deployed A2O2 projects with a 2-4 reflux ratio.this non-reflux technique without sedimentation only consumed one half of the power and shrank down to one third in space.Also compared with the Methanol supplemental carbon sourced OA technique.the forehead anaerobic stage reduced the organic loading of the aerobic phase,COD removal was improved and the extra expense for Methallol was avoided.
机译:从淹没的厌氧和缺氧池中,这些池的横截面具有蜂窝状结构的纤维填充物,收集的出气再吹回到同一池中。好氧反应器是通过气举的膜生物反应器(MBR)回路中,活性污泥浓度高达10-12 gL-1。在中试过程中,开发了一种直接冷却废水的AOA工艺。第一厌氧相的出水分流了10%实验表明,对于进水平均为2450 mgL-1 CODcr和95 mgL-1 NH4 + -N,系统得到稳定的废水。 124 mgL-1 CODcr和9.8 mg L-1 NH4 + -N。与正在进行的大排量A2O2工程相比,回流比为2-4,这种无沉淀的无回流技术仅消耗了一半的功率并收缩缩小到三分之一的空间。前额厌氧阶段减少了好氧阶段的有机负荷,提高了COD的去除率,避免了美索洛尔的额外支出。

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