Pollice A, Laera G
CNR-IRSA, Viale F. De Blasio 5, 70123 Bari, Italy.
Water Sci Technol. 2005;52(10-11):369-75.
The work reports the main results of an experimental activity aimed at evaluating the performance of a membrane bioreactor with complete sludge retention and the characteristics of its biomass. The bench scale system was started-up without any sludge inoculum and fed on real municipal sewage in order to favour biomass selection based on the imposed operating conditions. Process performance was evaluated in terms of COD removal (above 90% on average) and nitrification under two pre-determined volumetric loading rates (0.8 and 1.7 gCOD L(react)(-1), d(-1) on average). The biomass was evaluated in terms of growth, accumulation of inert solids, and bacterial activity. The latter was measured through respirometric tests. The results showed that the suspended solids concentrations (SS) under equilibrium were proportional to the volumetric loading rates in both the experimental periods considered and a relationship between these two parameters was proposed. Also, the organic loading rates reached the same equilibrium value of 0.12 gCOD gTSS(-1) d(-1) in the two periods. Moreover, the system showed very limited sludge production under equilibrium conditions (0.12 gVSS gCOD(rem)(-1) and low biomass activity, although it readily responded to load variations.
该工作报告了一项实验活动的主要结果,该活动旨在评估具有完全污泥截留功能的膜生物反应器的性能及其生物质特性。该实验室规模的系统在未接种任何污泥的情况下启动,并以实际城市污水为进料,以便根据设定的运行条件促进生物质的选择。在两种预定的体积负荷率(平均分别为0.8和1.7 gCOD L(反应)(-1) d(-1))下,根据化学需氧量去除率(平均高于90%)和硝化作用对工艺性能进行了评估。从生长、惰性固体积累和细菌活性方面对生物质进行了评估。后者通过呼吸测定试验进行测量。结果表明,在所考虑的两个实验阶段中,平衡状态下的悬浮固体浓度(SS)与体积负荷率成正比,并提出了这两个参数之间的关系。此外,两个阶段的有机负荷率均达到了相同的平衡值0.12 gCOD gTSS(-1) d(-1)。此外,该系统在平衡条件下污泥产量非常有限(0.12 gVSS gCOD(去除)(-1)),生物质活性较低,尽管它对负荷变化反应迅速。