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A novel anaerobic-anoxicitrifying-induced crystallization sequence batch reactor (A(2)N-IC-SBR) process for enhancing phosphorus recovery and nutrient removal

机译:一种新型的厌氧-厌氧/硝化诱导结晶顺序分批反应器(A(2)N-IC-SBR)工艺,用于提高磷的回收率和营养物的去除

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An anaerobic-anoxicitrifying-induced crystallization sequence batch reactor (A(2)N-IC-SBR) process was developed for enhanced nutrient removal and phosphorus recovery. The performance of the A(2)N-IC-SBR process was investigated in this study. Compared to the A(2)N-IC continuous flow (CF) process, A(2)N-IC-SBR provided important advantages, including minimal space requirements, ease of enhanced phosphorus recovery, and improved ammonia removal. Percentage of chemical phosphorus removal of total phosphorus removal was 14.9-17.1% in the A(2)N-IC-SBR process, while it was 8.0-12.6% in the A(2)N-IC-CF. The effluent ammonia concentrations were below 5 mg/L. The A(2)N-IC-SBR process met the requirements of Urban Waste Water Treatment Directive 91/271/EEC. Furthermore, ammonia and nitrate concentrations could be simulated satisfactorily in each stage. In addition, an important feature called the self-adjustment characteristic was found, as the system has the ability to cushion the effect of increased or decreased chemical phosphorus removal amount during the process.
机译:开发了厌氧-缺氧/硝化诱导结晶顺序分批反应器(A(2)N-IC-SBR)工艺,以提高营养物的去除和磷的回收率。在这项研究中研究了A(2)N-IC-SBR工艺的性能。与A(2)N-IC连续流(CF)工艺相比,A(2)N-IC-SBR提供了重要的优势,包括最小的空间要求,易于提高的磷回收率和改进的氨去除率。在A(2)N-IC-SBR工艺中,化学除磷率占总磷去除率的14.9-17.1%,而在A(2)N-IC-CF中为8.0-12.6%。出水氨浓度低于5 mg / L。 A(2)N-IC-SBR工艺符合城市废水处理指令91/271 / EEC的要求。此外,在每个阶段都可以令人满意地模拟氨和硝酸盐的浓度。此外,还发现了一个重要的特征,称为自我调节特性,因为该系统具有缓冲过程中化学除磷量增加或减少的作用的能力。

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