河海大学 环境学院,南京,210098
纸质出版:2012
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许航, 陈卫, 孙敏, 等. 两种膜的前端处理技术减缓膜污染的试验研究[J]. 土木与环境工程学报(中英文), 2012,34(1):108-112.
XU Hang, CHEN Wei, SUN Min, et al. Effect of Two Pretreatment Techniques on Preventing Membrane Fouling[J]. Journal of Civil and Environmental Engineering, 2012, 34(1): 108-112.
许航, 陈卫, 孙敏, 等. 两种膜的前端处理技术减缓膜污染的试验研究[J]. 土木与环境工程学报(中英文), 2012,34(1):108-112. DOI: 10.11835/j.issn.1674-4764.2012.01.021.
XU Hang, CHEN Wei, SUN Min, et al. Effect of Two Pretreatment Techniques on Preventing Membrane Fouling[J]. Journal of Civil and Environmental Engineering, 2012, 34(1): 108-112. DOI: 10.11835/j.issn.1674-4764.2012.01.021.
通过超滤膜过滤粉末活性炭预处理长江水和混凝沉淀预处理太湖水的上清液试验
比较各工艺中有机物极性含量的变化
结合膜的扫描电镜照片
探讨粉末活性炭和混凝沉淀预处理技术对膜污染的减缓作用。结果表明
疏水性有机物是造成膜污染的主要因素
亲水性有机物对膜污染的影响较小。超滤膜分别过滤经20 mg/L投量的粉末活性炭预处理的长江水样和25 mg/L投量的聚合氯化铝预处理的太湖水样时
相比直接过滤2种原水
超滤膜反洗后膜通量可有效恢复。粉末活性炭和混凝沉淀预处理后
膜表面形成的滤饼层较松散
易被周期性反洗排出膜组件
滤饼层可阻止疏水性有机物直接沉积在膜表面
减缓超滤膜污染
同时也可提高超滤膜出水的化学安全性。
Ultrafiltration membrane was used to filter the Yangtze River water by powder activated carbon (PAC) pretreated
such as Tai Lake water by coagulation-sedimentation pretreatment. The changes of organic polar content were compared in each process. Combined with the scanning electron microscope(SEM) photographs of the membrane
the mechanism of slowing down membrane fouling by PAC and coagulation-sedimentation pretreatment was studied. The results showed that hydrophobic organic compounds were the main factors of membrane fouling
while hydrophilic organics had less impact. When the dosing quantity of PAC filtered by ultrafiltration membrane was 20 mg/L to pre-treat the water samples of Yangtze River
and that of polyaluminium chloride was 25 mg/L for the pretreatment of Tai Lake water samples
the flux could be recovered effectively after backwashing compared with filtering the two raw water directly. The cake layer formed on the surface of the membrane was looser after pretreatment
and could be discharged easily by periodic backwashing
The cake layer could prevent hydrophobic organic matters deposit on the surface of membrane directly
which will slow down the membrane fouling and improve the chemical safety of the membrane effluent.
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