Water and Environmental Research and Study Centre, University of Jordan, Amman, Jordan.
J Environ Sci Health A Tox Hazard Subst Environ Eng. 2010 Jan;45(9):1054-9. doi: 10.1080/10934529.2010.486329.
Lamella settlers were used to increase sludge concentration in pilot scale UASB reactors treating concentrated sewage at low temperature. The aim was to increase sludge retention time (SRT) and achieve better digestion in UASB reactors without the need for increasing the hydraulic retention time (HRT). Two modified UASB reactors were used for this purpose. In the first reactor, lamella settlers were installed in the settling zone of the UASB reactor and the reactor was named UASB-ESR1. In the second reactor, lamella settlers were installed underneath the gas liquid separator (GLS) and the reactor was named UASB-ESR2. The sludge concentration, sludge profile, and system performance of each reactor were monitored. The obtained sludge concentrations were 50 and 53 g TS/l for UASB-ESR1 and UASB-ESR2, respectively. The measured concentrations were almost double the concentrations reported for conventional UASB reactors ranging 16-26 g TS/l. The calculated SRT in the modified UASB reactors was 103 days in both reactors. The average total COD (COD(tot)) and suspended COD (COD(ss)) removal efficiencies were 38% and 60%, respectively for the UASB-ESR1. The average COD(tot) and COD(ss) removal efficiencies for the UASB-ESR2 were 41% and 62%, respectively. The modified reactors were considered at the startup period and the performances of the modified systems are expected to significantly improve when arriving at steady state conditions.
采用斜板沉淀器来提高中温条件下处理浓缩污水的升流式厌氧污泥床(UASB)反应器中的污泥浓度。目的是在不增加水力停留时间(HRT)的情况下,通过增加污泥停留时间(SRT)来提高 UASB 反应器中的消化效果。为此使用了两个改良的 UASB 反应器。在第一个反应器中,斜板沉淀器安装在 UASB 反应器的沉淀区,该反应器被命名为 UASB-ESR1。在第二个反应器中,斜板沉淀器安装在气液分离器(GLS)下方,该反应器被命名为 UASB-ESR2。监测每个反应器的污泥浓度、污泥分布和系统性能。获得的污泥浓度分别为 UASB-ESR1 和 UASB-ESR2 的 50 和 53 g TS/L。测量的浓度几乎是传统 UASB 反应器报告的浓度的两倍,范围为 16-26 g TS/L。在改良的 UASB 反应器中计算的 SRT 为 103 天。UASB-ESR1 的平均总 COD(COD(tot)) 和悬浮 COD(COD(ss))去除效率分别为 38%和 60%。UASB-ESR2 的平均 COD(tot)和 COD(ss)去除效率分别为 41%和 62%。改良的反应器被认为处于启动阶段,当达到稳定状态条件时,改良系统的性能预计会有显著提高。