Cranfield University, Cranfield, Bedfordshire MK43 0AL, UK.
Water Res. 2013 Sep 15;47(14):4853-60. doi: 10.1016/j.watres.2013.05.008. Epub 2013 Jun 11.
The treatment efficiency and membrane performance of a granular and suspended growth anaerobic membrane bioreactor (G-AnMBR and AnMBR respectively) were compared and evaluated. Both anaerobic MBRs were operated in parallel during 250 days with low strength wastewater and under UK weather conditions. Both systems presented COD and BOD removal efficiencies of 80-95% and >90% respectively. Effluent BOD remained between 5 and 15 mgBOD L(-1) through the experimental period while effluent COD increased from 25 mg L(-1) to 75 mg L(-1) as temperature decreased from 25 °C to 10 °C respectively indicating the production of non biodegradable organics at lower temperatures. Although similar levels of low molecular weight organics were present in the sludge supernatant, recycling of the mixed liquor from the membrane tank to the bioreactor at a low upflow velocity enhanced interception of solids in the sludge bed of the G-AnMBR limiting the solid and colloidal load to the membrane as compared to the suspended system. Results from flux step test showed that critical flux increased from 4 to 13 L m(-2) h(-1) and from 3 to 5 L m(-2) h(-1) with gas sparging intensities varying from 0.007 m s(-1) to 0.041. Additional long term trials in which the effect of gas sparging rate and backwashing efficiency were assessed confirmed the lower fouling propensity of the G-AnMBR.
比较和评估了颗粒和悬浮生长厌氧膜生物反应器(G-AnMBR 和 AnMBR)的处理效率和膜性能。在英国天气条件下,两个厌氧 MBR 在 250 天的时间内以低强度废水运行,彼此平行。两个系统的 COD 和 BOD 去除效率分别为 80-95%和>90%。在整个实验期间,出水 BOD 保持在 5-15mgBOD/L 之间,而出水 COD 从 25mg/L 增加到 75mg/L,这表明在较低温度下会产生不可生物降解的有机物。尽管污泥上清液中存在相似水平的低分子量有机物,但在低上流速度下将混合液从膜槽循环回生物反应器,可以增强污泥床中固体的截留,与悬浮系统相比,限制了固体和胶体对膜的负荷。通量阶跃测试的结果表明,临界通量从 4L/m2h 增加到 13L/m2h,而从 3L/m2h 增加到 5L/m2h,气体曝气强度从 0.007m/s 增加到 0.041m/s。进一步进行了长期试验,评估了气体曝气速率和反冲洗效率的影响,证实了 G-AnMBR 的较低污染倾向。