Seccion de Ingenieria Quimica, Facultad de Ciencias, Universidad Autonoma de Madrid, C/ Francisco Tomas y Valiente 7, 28924, Madrid, Spain.
Water Res. 2016 Nov 15;105:65-75. doi: 10.1016/j.watres.2016.08.059. Epub 2016 Aug 30.
The potential application of powdered activated carbon (PAC) to mitigate membrane fouling has been tested in membrane bioreactors (MBRs) fed with cosmetic wastewater. Inexpensive powder activated carbon was prepared from sewage sludge biosolids (B-PAC) by pyrolysis (750 °C; 0.5 h) and air-activation (400 °C; 2 h). Adsorption capacities of 143 and 570 mg g were reached for carbohydrates and proteins, respectively, quite similar to those of a commercial activated carbon (C-PAC). To check the effect of PAC addition on membrane fouling, three MBRs were simultaneously operated without (control-MBR) and with PAC (B-MBR and C-MBR) for 150 days in continuous mode at 8 L m h flux. Similar COD removal efficiencies were achieved in these three MBR systems. After 100 days of operation, the effect of the PACs on the sludge filterability was studied in the MBRs for 10 days. B-MBR showed stable transmembrane pressure (TMP) after 9 days of operation, unlike of control-MBR and C-MBR, where the TMP increased after the 2nd and 5th days, respectively. Therefore, operational cost saving can be achieved in the membrane cleaning due to decrease of fouling rate. Operating at stable state condition the addition of PAC gave rise to an increase of the critical flux of 25%. In an extra shear test, carried out at the end of the continuous experiment, a clear reduction in mean size of the flocs from 45 to 28 μm was observed in control-MBR. However, the extra shear led to a slight reduction of the mean size of flocs (less than 5%) in MBRs with PAC, with average sizes of 62 and 71 μm in C-MBR and B-MBR, respectively. The molecular weight fractionation of the MBR demonstrated a higher selectivity of B-PAC toward the adsorption of proteins smaller than 1 μm which prevents the irreversible fouling of the membranes. The membranes lifetime was increased because the B-PAC extended the filtration for a longer period than C-PAC, probably due to its easier in-situ regeneration.
粉末活性炭(PAC)在膜生物反应器(MBR)中应用于减轻膜污染的潜力已在以化妆品废水为食的 MBR 中进行了测试。通过热解(750°C;0.5 小时)和空气活化(400°C;2 小时),从污水污泥生物固体(B-PAC)中制备了廉价的粉末活性炭。对于碳水化合物和蛋白质,B-PAC 的吸附容量分别达到了 143 和 570mg/g,与商业活性炭(C-PAC)相当。为了检查 PAC 添加剂对膜污染的影响,在连续模式下以 8L/mh 的通量连续运行三个 MBR 150 天,一个没有(对照-MBR)和两个添加了 PAC(B-MBR 和 C-MBR)。在这三个 MBR 系统中均实现了相似的 COD 去除效率。在运行 100 天后,在 MBR 中研究了 PAC 对污泥过滤性能的影响,为期 10 天。与对照-MBR 和 C-MBR 不同,B-MBR 在运行 9 天后稳定的跨膜压力(TMP),在第 2 天和第 5 天分别增加了 TMP。因此,由于减少了污染速率,在膜清洗中可以节省运行成本。在稳定状态下运行时,PAC 的添加使临界通量增加了 25%。在连续实验结束时进行的额外剪切试验中,在对照-MBR 中观察到絮体的平均粒径从 45μm 明显减小到 28μm。然而,额外的剪切导致 PAC 存在的 MBR 中的絮体平均尺寸略有减小(小于 5%),在 C-MBR 和 B-MBR 中的平均尺寸分别为 62μm 和 71μm。MBR 的分子量分级表明,B-PAC 对小于 1μm 的蛋白质的吸附具有更高的选择性,这可以防止膜的不可逆污染。由于 B-PAC 比 C-PAC 更易于原位再生,因此延长了过滤时间,从而延长了膜的使用寿命。