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A novel anaerobic filter membrane bioreactor: prototype start-up and filtration assays

机译:一种新型厌氧过滤膜生物反应器:原型启动和过滤测定

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Anaerobic digestion allows efficient treatment of high loaded wastewater, and membrane technology allows obtaining high quality effluents with complete biomass retention. However, high biomass concentration interferes with membrane fouling. In the present work, a new bioreactor that integrates an attached biomass anaerobic culture on a fixed bed and a submerged membrane has been started up. The recirculation between the digestion and filtration chambers is coupled to the gas-lift effect of the bubbling employed for the scouring of the membranes, avoiding the use or electromechanical pumps that damage the suspended biomass. The support material retains the biomass in the digestion tank despite the downwards flow, avoiding the submerged membrane contacting with a high concentrated suspension. This novel system, called an anaerobic filter membrane bioreactor was immediately started up, achieving chemical oxygen demand (COD) removal efficiencies of 96% at an organic loading rate (OLR) of 7 kg COD/m(3).d. In order to select filtration flux, specific gas demand and filtration cycle duration, the results of 15 short term assays, eight hours for each one, is presented for fluxes between 15.7 and 17.7 L/m(2).h, cycle duration between 10 and 30 minutes, and three levels of scouring. It was checked that reversible and irreversible fouling were directly related when dTMP/dt 2.5 mbar/min.
机译:厌氧消化允许高负荷废水的有效处理,膜技术允许获得具有完全生物质保留的高质量污水。然而,高生物量浓度干扰了膜污染。在本作工作中,启动了一种新的生物反应器,其在固定床和浸没膜上整合了附着的生物量厌氧培养物。消化和过滤室之间的再循环耦合到用于冲洗膜的鼓泡的气体升力效果,避免损坏悬浮生物质的使用或机电泵。尽管向下流动,载体材料在消化罐中保留生物质,避免浸没膜与高浓缩悬浮液接触。这种新的系统,称为厌氧过滤膜生物反应器立即启动,在7kg COD / m(3)的有机加载速率(OLR)下实现化学需氧量(COD)去除效率为96%。为了选择过滤通量,特定的气体需求和过滤循环持续时间,在15.7和17.7L / m(2).h之间的助熔剂,在15.7和17.7L / m(2).h之间的助熔剂,循环持续时间为15个短术语测定,八小时的15小时的结果。和30分钟,三个水平。检查了DTMP / DT&GT的可逆和不可逆转的污垢直接相关; 2.5毫巴/分钟。

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