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Fouling resistant compact hollow-fiber module with spacer for submerged membrane bioreactor treating high strength industrial wastewater

机译:带有隔板的防污紧凑型中空纤维组件,用于水下膜生物反应器处理高强度工业废水

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摘要

Long-term investigations carried out in a submerged membrane fungi reactor treating textile wastewater revealed the excellent fouling prevention capacity of spacer-filled hollow-fiber modules. The type and arrangement of the spacers governed the overall rigidity of the modules and played the critical role in avoidance of sludge intrusion and retrieval of the original state (cleaning). A hybrid module (fiber packing density = 61.5%, surface area = 1.07 m2) obtained by winding a rigid spacer (thickness = 1 mm, opening = 7 mm × 7 mm) on the surface of a module originally containing a flexible thin spacer (opening = 1 mm × 1 mm) exhibited the optimum rigidity so as to minimize intrusion of sludge while simultaneously allowing washout of the small amount of sludge trapped within it. Periodic in situ chemical backwashing with a small dose (500 mg Cl L−1, 100 mL m−2, twice/week) and intermittent surface-cleaning with a specially designed aeration device (aeration intensity = 1 L min−1, duration = 1 min per 30 min) enabled stable operation for a prolonged period under the selected average flux (1.27 × 10−7 m3 m−2 s−1) and mixed liquor suspended solids (MLSS) concentrations (up to 25 g L−1). Under the similar conditions, four-fold reduction in total consumptions of both chemical and air was possible when the developed module was placed within a coarse-pore (50–200 μm) pre-filtration cage. A reactor-design with a settling zone and a feeding mode comprising split of the influent through the settling zone and from the top may be utilized to maintain an optimum MLSS concentration in direct contact with the membrane, thereby further improving the ease of fouling mitigation.
机译:在浸没式膜真菌反应器中对纺织品废水进行的长期研究表明,填充垫片的中空纤维组件具有出色的防污能力。垫片的类型和布置控制着模块的整体刚度,并在避免污泥侵入和恢复原始状态(清洁)方面发挥了关键作用。通过将刚性垫片(厚度= 1 mm,开口= 7 mm×7 mm)缠绕在最初包含柔性薄垫片(模块)的模块表面上而获得的混合模块(纤维堆积密度= 61.5%,表面积= 1.07 m2)开口= 1 mm×1 mm)表现出最佳的刚度,从而最大程度地减少了污泥的侵入,同时还可以冲洗掉残留在其中的少量污泥。小剂量(500 mg Cl L-1、100 mL m-2,每周两次)的定期原位化学反冲洗,并使用专门设计的曝气设备进行间歇性表面清洁(曝气强度= 1 L min-1,持续时间=每30分钟1分钟)在选定的平均通量(1.27×10-7 m3 m-2 s-1)和混合液悬浮固体(MLSS)浓度(最高25 g L-1)下可以长时间稳定运行。在相似的条件下,将开发的模块放置在粗孔(50-200μm)的预过滤笼中时,化学和空气的总消耗量可以减少四倍。具有沉降区和进料模式的反应器设计包括通过沉降区并从顶部分流的进料,可用于维持与膜直接接触的最佳MLSS浓度,从而进一步提高减轻结垢的容易性。

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