Department of Civil and Environmental Engineering, University of Massachusetts, Amherst, MA 01003, USA.
Water Res. 2011 Nov 15;45(18):6021-9. doi: 10.1016/j.watres.2011.08.051. Epub 2011 Sep 6.
To investigate the mechanism of sludge reduction in the anaerobic side-stream reactor (SSR) process, activated sludge with five different sludge reduction schemes were studied side-by-side in the laboratory. These are activated sludge with: 1) aerobic SSR, 2) anaerobic SSR, 3) aerobic digester, 4) anaerobic digester, and 5) no sludge wastage. The system with anaerobic SSR (system #2) was the focus of this study and four other systems served as control processes with different functions and purposes. Both mathematical and experimental approaches were made to determine solids retention time (SRT) and sludge yield for the anaerobic SSR process. The results showed that the anaerobic SSR process produced the lowest solids generation, indicating that sludge organic fractions degraded in this system are larger than other systems that possess only aerobic or anaerobic mode. Among three systems that involved long SRT (system #1, #2, and #5), it was only system #2 that showed stable sludge settling and effluent quality, indicating that efficient sludge reduction in this process occurred along with continuous generation of normal sludge flocs. This observation was further supported by batch anaerobic and aerobic digestion data. Batch digestion on sludges collected after 109 days of operation clearly demonstrated that both anaerobically and aerobically digestible materials were removed in activated sludge with anaerobic SSR. In contrast, sludge reduction in the aerobic SSR process or no wastage system was achieved by removal of mainly aerobically digestible materials. All these results led us to conclude that repeating sludge under both feast/fasting and anaerobic/aerobic conditions (i.e., activated sludge with anaerobic SSR) is necessary to achieve the highest biological solids reduction with normal wastewater treatment performance.
为了研究厌氧侧流反应器 (SSR) 工艺中污泥减量化的机制,本研究在实验室中并排研究了具有五种不同污泥减量化方案的活性污泥。这些方案是:1) 好氧 SSR;2) 厌氧 SSR;3) 好氧消化池;4) 厌氧消化池;5) 无污泥流失。本研究的重点是具有厌氧 SSR 的系统(系统 #2),其他四个系统作为具有不同功能和目的的对照工艺。采用数学和实验方法确定了厌氧 SSR 工艺的固体停留时间 (SRT) 和污泥产率。结果表明,厌氧 SSR 工艺产生的固体生成量最低,表明该系统中降解的污泥有机部分大于其他仅具有好氧或厌氧模式的系统。在涉及长 SRT 的三个系统(系统 #1、#2 和 #5)中,只有系统 #2 表现出稳定的污泥沉降和出水水质,表明该过程中的高效污泥减量化伴随着正常污泥絮体的连续生成。这一观察结果得到了批式厌氧和好氧消化数据的进一步支持。对运行 109 天后收集的污泥进行的批式消化实验清楚地表明,在具有厌氧 SSR 的活性污泥中,同时去除了可厌氧和可好氧消化的物质。相比之下,在好氧 SSR 工艺或无污泥流失系统中实现的污泥减量化是通过去除主要可好氧消化的物质来实现的。所有这些结果使我们得出结论,即在好氧/缺氧和厌氧/好氧条件下重复污泥(即具有厌氧 SSR 的活性污泥)是实现最高生物固体减量化和正常废水处理性能的必要条件。