A hybrid membrane process for simultaneous thickening and digestion of waste activated sludge

A hybrid membrane process for simultaneous sludge thickening and digestion (MSTD) was studied. During one cycle (15 d) of operation under a hydraulic retention time of 1 d, the concentration of mixed liquor suspended solids (MLSS) continuously increased from about 4 g·L⁻¹ to 34 g·L⁻¹, and the mixed liquor volatile suspended solids (MLVSS) increased from about 3 g·L⁻¹ to over 22 g·L⁻¹. About 42% of the MLVSS and 39% of the MLSS reduction were achieved. The thickening and digestion effects in the MSTD were further analyzed based on a mass balance analysis. Test results showed that biopolymers and cations of biomass were gradually released to the bulk solution during the process. It was also found that the capillary suction time, colloidal chemical oxygen demand, soluble microbial products, viscosity, and MLSS had significant positive correlations with the membrane fouling rate, whereas extracellular polymeric substances, polysaccharides, and proteins extracted from biomass had negative impacts on membrane fouling.     

Estimation of fecal Coliform removal from domestic sewage in two sand filter column systems

The objective of the present research is to compare fecal coliform removal from two different sand column systems treating septic tank effluent over a range of hydraulic loading rates. Drain time measurements were performed to compare the hydraulic characteristic of the column systems at different hydraulic loading rates. Biochemical oxygen demand (BOD), total suspended solids (TSS), and pH were also measured for the septic tank effluent. A removal of the order of 99% for fecal coliform, TSS, and BOD in column effluent was achieved using the sand filter columns. The ‘break‐in’ period for determining the effectiveness of the sand filter columns is also discussed.     

气箱式脉冲袋式除尘器清灰技术

为了深入认识气箱式脉冲袋式除尘器的清灰机理,按可压缩气体绝热状态和等温状态分别计算了脉冲质量流量和气箱中气体压力、密度的变化,进一步推导出穿过滤袋的清灰气流速度方程和清灰剥离力方程.按照在袋式除尘器实验模型上所测定的粉尘剥离率与清灰剥离力之间的特性关系,确定了已知条件下的粉尘剥离率.若预先确定要求达到的粉尘剥离率,可以通过清灰气流速度方程和剥离力方程确定脉冲清灰系统的几何参数、脉冲喷吹压力、脉冲喷吹时间和分室内的过滤面积(或滤袋直径、滤袋长度和滤袋数量等).该理论和实验研究内容为气箱式脉冲袋式除尘器脉冲清灰系统设计计算提供了理论依据.     

基于EOS/MODIS影像的青海省一次典型沙尘事件遥感监测研究

基于2012年11月至12月上午轨道星Terra共7景MODIS数据,对影响青海省的一次典型沙尘事件进行研究。结果表明,沙尘天气始于2012年11月18日,在12月1日及2日达到高峰,持续到12月18日趋于减弱;沙尘天气影响区域范围较广,主要影响省域西北、东北地区,面积占省域面积的11.26%至43.36%;沙尘天气扩散趋势与路径整体上由西北向东北地区,东部人口密集区沙尘天气出现时间相对西北地区、青南高原地区出现滞后。     

氢氧化钠-膜过滤法处理含镍电镀废液

介绍了氢氧化钠－膜过滤法处理含镍电镀废液新工艺，并确定了主要的技术参数。该工艺具有回收NiSO4纯度高，出水Ni^2 可实现稳定达排放等优点。     

植物根过滤作用对重金属的富集研究

用作植物根的过滤作用来处理污水中的重金属是一种新兴的重金属污水植物处理技术。以陆生植物－萝卜块状根系为材料，通过溶液培养的方法，研究了根过滤作用对重金属的富集情况，为陆生植物在重金属污水净化中的应用提供理论依据。     

硅胶色层分析土壤中水溶性腐殖酸

采用水浸取法和硅胶色层法，通过紫外吸收光谱峰定性鉴定了英格兰七种土壤水溶性腐殖酸。沉积土中水溶性腐殖酸均展示了二组峰值，而在草原土中低分子量组份消失。选用γ谱仪测定了沉积土水溶性腐殖酸中的放射性核素^137Cs，采用中子活化测量技术分析了常量钠和氯。结果表明，在高盐含量的沉积土中存在的大量竞争络合离子钠可能是使放射性核素^137Cs与沉积土中水溶性腐殖酸没有直接关系的原因。     

应用生物强化活性滤池的滤料选择及效果

生物强化活性滤池是一种经济有效的给水处理工艺,可去除约90％的AOC,保证出水的生物稳定性。滤料的选择应用是构建生物强化活性滤池的基础,直接影响了生物活性滤池内富集的生物量和出水水质。本文着重从滤料的角度,探讨了在构建和运行生物强化活性滤池过程中应予以注意的问题。     

EFFECT OF FILTRATION PRESSURE ON ANALYSES FOR CHLOROPHYLL1

ABSTRACT: Nine samples, each with different kinds and numbers of algae, were filtered at five pressures from 5 to 75 pounds per square inch and the amounts of chlorophylls a and b were measured. Pressures in the range tested had no effect on the measured amounts.     

TCE recovery mechanisms using micellar and alcohol solutions: phase diagrams and sand column experiments

Forty-one phase diagrams and fifteen sand column experiments were conducted to evaluate the efficiency of three types of washing solutions to recover trichloroethylene (TCE) at residual saturation and to identify the recovery mechanisms involved. This study demonstrates that: (1) an alcohol and a surfactant combination is more efficient than an alcohol used alone in water; (2) the prediction of the dominant recovery mechanism from the tie line slopes in phase diagram is accurate and can be reproduced in sand column experiments; and (3) TCE recovery efficiency in sand column experiments is generally well represented by the position of the miscibility curve in phase diagrams in the low concentration range. However, the miscibility curve alone is not sufficient to exactly predict the TCE recovery mechanisms involved. Tie line slopes and the critical tie line have to be taken into consideration to select the active matter as well as its concentration and to predict the dominant recovery mechanism in sand column experiments. The sand column experiments quantified the recovery efficiency of each solution and identified the proportion of the recovery mechanisms (mobilisation vs. solubilisation). Washing solutions with an active matter concentration above the critical tie line caused dominating mobilisation. Mobilisation was also dominant when the active matter of the washing solution partitioned into the organic phase and the active matter concentration was below the critical tie line. Solubilisation and emulsification were dominant for washing solutions containing active matter, which principally partitioned into the aqueous phase and an active matter concentration below the critical tie line.