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出水营养浓度:
为了达到满意的出水标准,最后操作的营养浓度标准及合适的操作更为重要。图3表明不同出水中的营养浓度。
表2中描述了各操作进水和出水中营养浓度和去除率。三步、四步和五步操作中出水COD浓度为28 mg L-1。明显的,四步操作的COD的去除率最低。三步和五步操作同样受到出水标准的限制。出水三步操作NH4-N的去除率最低(3.2 mg L-1)。但是,出水五步操作NH4-N的去除率最高(5.6 mg L-1)。最后NH4-N(0.9 mg L-1)和PO4-P的浓度(3.2 mg L-1)明显低于其他操作。因此,运用五步操作明显优于其它操作。

五步操作中的营养浓度数据:
五步操作在10.5-h中的营养浓度COD, NH4-N,NO3-N和PO4-P的数据见图4。COD浓度随着时间从632 mg L-1最后降到37 mg L-1。大多数COD是在最初的六小时期间降解的。最后两个操作过程中相对于COD,主要去除N和P。
NH4-N在最初的2.5 h (an和ax阶段)保持不变,在第一个好氧阶段由于同化和硝化作用而明显下降。NH4-N浓度在后两个过程中基本不变,操作在最后浓度为5.6 mg L-1。
COD, NH4-N,NO3-N不同变化,说明了不同操作中的变化趋势。NO3-N的降低是因为前两个阶段NO3-N的反硝化作用,但是在第一好氧阶段由于NH4-N的硝化作用而升高。在第二个间氧阶段,NO3-N的反硝化使得NO3-N浓度降到操作最后水平0.9 mg L-1。
P的去除主要在厌氧和间氧阶段去除,因此PO4-P在前两个操作阶段明显降低。但是在第一个和第二个好氧阶段有所上升。最后,PO4-P浓度接近于3.2 mg L-1低于比以前报道的7.4 mg L-1。

结论:
在运用不同SBR操作步骤来实现从模拟废水中去除营养。三步-(An/Ax/Ox)、四步- (An/Ox/
Ax/Ox) 五步 (An/Ax/Ox/Ax/Ox)操作在不同的操作时间下,并对其去除结果进行测定和比较。对COD和 NH4-N在不同的操作过程中进行比较,三步操作明显最好。这是因为大部分COD和 NH4-N在最初的三个步骤中去除的。但是,PO4-P和NO3-N的去除效果,五步操作高于其他操作。反硝化作用发生在第二个间氧阶段,多余的P是在第二个好氧阶段吸收,NO3-N和PO4-P在五步操作中明显高。最后,五步操作包括An/Ax/Ox/Ax/Ox阶段,操作时间分别为1/1.5/4/1.5/2 h,COD,NH4-N,NO3-N和PO4-P浓度降到37 mg L-1,5.6 mg L-1,0.9 mg L-1 和 3.2 mg L-1,去除了94%的COD、90%的NH4-N、64%NO3-N和PO4-P57%。
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