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通过生物沥浸提高城市污水污泥脱水性能:基于连续推流反应模型的中试研究

[Improvement of municipal sewage sludge dewaterability by bioleaching: a pilot-scale study with a continuous plug flow reaction model].

作者信息

Liu Fen-Wu, Zhou Li-Xiang, Zhou Jun, Jiang Feng

机构信息

Department of Environmental Engineering, College of Resources and Environmental Sciences, Nanjing Agricultural University, Nanjing 210095, China.

出版信息

Huan Jing Ke Xue. 2011 Oct;32(10):2993-8.

Abstract

A plug-flow bio-reactor of 700 L working volume for sludge bioleaching was used in this study. The reactor was operationally divided into six sections along the direction of the sludge movement. Ten duration of continuous operation of sludge bioleaching with Acidibacillus spp. and 1.2 m3 x h(-1) aeration amount was conducted. In this system, sludge retention time was 2.5 d, and the added amount of microbial nutritional substance was 4 g x L(-1). During sludge bioleaching, the dynamic changes of pH, dewaterability (specific resistance to filtration, SRF) of sewage sludge in different sections, the moisture content and moisture evaporation rate of dewatered bioleached sludge cake obtained by chamber filter press were investigated. The results showed that the SRF of sludge significantly decreased from initial 1.50 x 10(13) m x kg(-1) to the final 0.34 x 10(13) m x kg(-1). The wasted bioleached sludge was collected and dewatered by chamber filter press under the following pressures as 0.3 MPa for 4 h (2 h for feeding sludge, 2 h for holding pressure), 3 h (1.5 h for feeding sludge, 1.5 h for holding pressure), 2 h (1 h for feeding sludge, 1 h for holding pressure), and 1 h (0.5 h for feeding sludge, 0.5 h for holding pressure). Correspondingly, the moisture of dewatered sludge was reduced to 57.9%, 59.2%, 59.6%, and 63.4% of initial moisture, respectively. Moreover, the moisture content of bioleached sludge cake was reduced to about 45% and less than 10% if the cake was placed at 25 degrees C for 15 h and 96 h, respectively. Obviously, sludge bioleaching followed by sludge dewatering using chamber filter press is a promising attractive approach for sludge half-dryness treatment in engineering application.

摘要

本研究采用了一个工作体积为700 L的推流式生物反应器用于污泥生物沥浸。该反应器沿污泥移动方向在运行上被分为六个部分。进行了以嗜酸菌属进行的污泥生物沥浸连续运行10个周期,曝气量为1.2 m³·h⁻¹。在该系统中,污泥停留时间为2.5 d,微生物营养物质添加量为4 g·L⁻¹。在污泥生物沥浸过程中,研究了不同部分污泥的pH值、脱水性能(过滤比阻,SRF)的动态变化,以及厢式压滤机所得脱水生物沥浸污泥饼的含水率和水分蒸发速率。结果表明,污泥的SRF从初始的1.50×10¹³ m·kg⁻¹显著降低至最终的0.34×10¹³ m·kg⁻¹。将废弃的生物沥浸污泥收集起来,通过厢式压滤机在以下压力下进行脱水:0.3 MPa下4 h(进料污泥2 h,保压2 h)、3 h(进料污泥1.5 h,保压1.5 h)、2 h(进料污泥1 h,保压1 h)和1 h(进料污泥0.5 h,保压0.5 h)。相应地,脱水污泥的含水率分别降至初始含水率的57.9%、59.2%、59.6%和63.4%。此外,如果将生物沥浸污泥饼分别在25℃下放置15 h和96 h,其含水率分别降至约45%和低于10%。显然,污泥生物沥浸后再通过厢式压滤机进行污泥脱水,在工程应用中是一种很有前景的污泥半干化处理方法。

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