饮用水超滤膜处理中试中的膜污染控制 |
作者:朱丹 ,顾平1*,王海燕1,何凤华2,韩涛2 |
单位: 1.天津大学 环境科学与工程学院,天津 300072;2.天津泰达自来水公司,天津 300457 |
关键词: 饮用水;膜污染;反洗;化学强化反洗(CEB);化学清洗;预氯化 |
DOI号: |
分类号: TU 991.2 |
出版年,卷(期):页码: 2012,32(4):81-86 |
摘要: |
采用中试规模的压力式超滤膜系统处理水厂的沉淀池出水,对试验期间的膜污染控制技术进行了研究。试验中采用了物理反洗,化学强化反洗(CEB),化学清洗和预氯化对膜污染进行控制。结果表明:物理反洗工艺对于膜污染的去除效果不明显;CEB是一种物理和化学方法相结合的在线清洗方法,能够有效地恢复膜比通量,平均恢复率达85 %;采用草酸进行化学清洗效果较好,4次清洗膜比通量平均提高了265 L/(h•m2•bar)。对膜反洗水的成分分析表明:铁和溶解性有机物是导致中试系统膜污染的主要因素。预氯化可以有效地减缓膜污染速率。 |
A pilot-scale low pressure ultrafiltration membrane system was used to treat the finished water from a sedimention tank in the waterworks, and membrane fouling control was investigated. Physical backwashing, chemical enhanced backwash (CEB), chemical cleaning and pre-chlorination were studied for membrane fouling control. Results showed that physical backwashing have a little effect on fouling control, however, CEB, an online cleaning mode could have a great effect on fouling control, and the average recovery rate of specific flux was 85%. The effect of chemical cleaning with oxalic acid was better, after cleaning, the average SF value was increased to 265 L/(h•m2•bar). Pre-chlorination could slow down the fouling rate. In addition, the composition of the eluent was analysed. The results revealed that iron and dissolved organic matter were the major factors for fouling. |
基金项目: |
作者简介: |
朱丹(1987-),女,陕西宝鸡,硕士研究生,从事饮用水膜法处理研究。 *通讯联系人,022-27405059, |
参考文献: |
[1] 刑卫红, 童金忠, 王焕章, 等. 微滤和超滤过程中浓差极化和膜污染控制方法研究[J]. 化工进展, 2000(1): 44-48. [2] Musale D A, Kulkami S S. Fouling reduction in poly(aerylonitrile-co-acrylamide) ultrafiltration membranes[J]. Journal of Membrane Science, 1996, 111(1): 49-56. [3] 张博丰, 马世虎. 超/微滤膜的膜污染与膜清洗研究[J]. 供水技术, 2009, 3(6): 13-16. [4] 沈悦啸, 王利政, 莫颖慧, 等. 膜污染和膜材料的最新研究进展[J]. 中国给水排水, 2010, 26(14): 16-22. [5] Yoon S H, Kim H S, Yeom I T. Optimization model of submerged hollow fiber membrane modules[J]. Journal of Membrane Science, 2004, 234(1-2): 147-156. [6] Chang S, Fane A G. Filtration of biomass with laboratory scale submerged hollow fibre modules: effect of operating conditions and module configuration[J]. Journal of Chemical Technology and Biotechnology, 2002, 77(9): 1030-1038. [7] 董秉直, 刘凤仙, 桂 波. 在线混凝处理微污染水源水的中试研究[J]. 工业水处理, 2008, (1): 40-43. [8] 罗 虹, 顾 平, 杨造燕. 投加粉末活性炭对膜阻力的影响研究[J]. 中国给水排水, 2001, 17(2): 1-4. [9] Heng Liang, Yanglin Yang, Weijia Gong, et al. Effect of pretreatment by permanganate/chlorine on algae fouling control for ultrafiltration(UF) membrane system[J]. Desalination, 2008, 222(1-3): 74-80. [10] Shimizu Y, Okuno Y, Uryu K, et al. Filtration characteristics of hollow fiber microfiltration membranes used in membrane bioreactor for domestic wastewater treatment[J]. Water Research, 1996, 30(10): 2285-2392. [11] 王 湛. 膜分离技术基础[M]. 北京:化学工业出版社, 2000. [12] Faust S D, Aly O. Chemistry of Water Treatment[M]. USA: CRC, 1998. [13] Lee H, Amy G, Cho J, et al. Cleaning strategies for flux recovery of an ultrafiltration membrane fouled by natural organic matter[J]. Water Research, 2001, 35(14): 3301-3308. [14] Al-Amoudi A, Lovitt R W. Fouling strategies and the cleaning system of NF membranes and factors affecting cleaning efficiency[J]. Journal of Membrane Science, 2007, 303(1-2): 4-28. [15] Thurman E M. Organic Geochemistry of Natural Waters[M]. USA: Kluwer Academic Publishers, 1985. [16] Arnal J M, Garcia-Fayos B, Sancho M, et al. Cleaning ultrafiltration membranes by different chemical solutions with air bubbles[J]. Desalination and Water Treatment, 2009, 10(1-3): 175-180. [17] 董秉直, 曹达文, 陈 艳. 饮用水膜深度处理技术[M]. 北京:化学工业出版社, 2006. [18] Strugholtz S, Sundaramoorthy K, Panglisch S, et al. Evaluation of the performance of different chemicals for cleaning capillary membranes[J]. Desalination, 2005, 179(1-3): 191-202. [19] Yinghui Mo, Jianhua Chen, Wenchao Xue, et al. Chemical cleaning of nanofiltration membrane filtrating the effluent from a membrane bioreactor[J]. Separation and Purification Technology, 2010, 75(3): 407-411. [20] 张玲玲. 混凝-微滤工艺制备饮用水的试验研究[D]: [学位论文].天津: 天津大学环境科学与工程学院, 2008. [21] Choo K H, Lee H, Choi S J. Iron and manganese removal and membrane fouling during UF in conjunction with prechlorination for drinking water treatment[J]. Journal of Membrane Science, 2005, 267(1-2): 18-26. [22] Chang Y J, Choo K H, Benjamin M M, et al. Combined adsorption/UF process increases TOC removal[J]. Journal of the American Water Works Association, 1998, 90(5): 90-102. |
服务与反馈: |
【文章下载】【加入收藏】 |
《膜科学与技术》编辑部 地址:北京市朝阳区北三环东路19号蓝星大厦 邮政编码:100029 电话:010-64426130/64433466 传真:010-80485372邮箱:mkxyjs@163.com
京公网安备11011302000819号