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Understanding the influence of operating parameters throughin silicooptimization of energy consumption of submerged membrane bioreactor for urban wastewater treatment

机译:通过计算机优化沉膜生物反应器能耗来优化城市污水处理,了解操作参数的影响

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摘要

Membrane bioreactor technology has become relatively widespread as an advanced treatment for both industrial and municipal wastewaters. The main problem of these installations is that they do not operate at the maximum of their potential, mainly because of membrane fouling. Experimental research with this kind of installation requires resources and is time consuming. The use of a computer simulator, as in the present work, allows the fouling behaviour in a bench-scale submerged membrane bioreactor to be investigated over a wide range of operating parameters: average specific aeration intensity (0.041–0.277 L m−2 s−1), filtration flux (0.032–0.160 m3 m−2 d−1) and filtration and coarse bubble aeration cycles (filtration and aeration times: 60–1080 s, with/without ratio: 0.33/10). A quadratic optimization method applied to the energy consumption (EC) was first carried out: minimum values of 0.27 and 0.32 kW h m−3 were obtained for EC in the sequential and non-sequential operating modes, respectively. Using the optimal operating conditions and the most influent parameters found in the first part, the second part details their influence on both membrane fouling and EC for each operating mode. The mean filtration flux and the mean aeration intensity have opposite effects on fouling and EC, which implies that a more global, economic optimization, including chemical cleaning, is needed. The detailed study of filtration and coarse bubble aeration cycles showed that they had little influence for a with/without ratio superior to 1. Using the quadratic optimization method with in silico experiments gave reliable first approximation results.
机译:膜生物反应器技术已经作为一种工业和市政废水的高级处理方法而相对普及。这些装置的主要问题是,由于膜污染,它们无法发挥最大的潜力。使用这种安装进行实验研究需要资源并且很耗时。如目前的工作一样,使用计算机模拟器可以在广泛的工作参数范围内研究台式规模的浸没式膜生物反应器中的结垢行为:平均比曝气强度(0.041–0.277 L m−2 s− 1),过滤通量(0.032–0.160 m3 m-2 d-1),过滤和粗气泡曝气循环(过滤和曝气时间:60–1080 s,有/无比率:0.33 / 10)。首先执行应用于能量消耗(EC)的二次优化方法:在顺序和非顺序运行模式下,EC的最小值分别为0.27和0.32 kW h m-3。使用第一部分中发现的最佳操作条件和最有影响力的参数,第二部分详细介绍了它们对每种操作模式对膜污染和EC的影响。平均过滤通量和平均通气强度对结垢和EC产生相反的影响,这意味着需要更全面,更经济的优化,包括化学清洗。对过滤和粗气泡曝气循环的详细研究表明,对于有/无比大于1的情况,它们几乎没有影响。使用二次优化方法和计算机模拟实验可得出可靠的第一近似结果。

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