超滤膜处理稀土冶炼废水过程膜污染特性分析
作者:桂双林1,麦兆环,付嘉琦,魏源送3,陈小平2,万金保1
单位: 1.南昌大学鄱阳湖环境与资源利用教育部重点实验室,资源环境与化工学院,南昌 330031;2.江西省科学院能源研究所,南昌 330096;3.中国科学院生态环境研究中心,水污染控制实验室,北京 100085
关键词: 超滤;稀土冶炼;膜污染;废水处理
出版年,卷(期):页码: 2020,40(5):77-84

摘要:
采用超滤膜错流过滤稀土冶炼萃取废水,对污染物的处理效率和膜污染特征进行了研究。通过设计膜阻构成实验,测算膜污染总阻力及其构成比例,结果表明膜自身阻力(Rm)相对较高,膜污染阻力以沉积层阻力(Rc)和堵塞阻力(Rf)为主,浓差极化阻力(Rp)较弱。考察了膜通量随时间和跨膜压差变化规律,以及超滤膜对污染物的截留效率,当跨膜压差为0.1-0.5MPa时,COD和浊度平均去除率分别为26.5%和77.7%。SEM-EDX分析发现膜面有大量颗粒物和结晶物等污染物,Na、Ca、Cl和S为主要无机元素。采用纯水、HCl、NaOH、NaClO和EDTA五种清洗液对污染膜进行了清洗,对洗脱液组成、污染膜和清洗膜的形貌特征进行了分析,结果表明酸洗对无机金属离子有着较好的去除效果,碱洗对有机物尤其是腐殖酸类和芳香族化合物的去除效果较佳。
In this study, the UF membrane was used to treat rare earth smelting wastewater by cross-flow filtration. The treatment efficiency and the characteristics of fouled membrane were studied. Then the total resistance of the membrane fouling and its composition were calculated.
The results showed that the proportions of membrane intrinsic resistance (Rm) was relatively high.
Membrane fouling resistance was mainly composed by cake layer resistance (Rc) and pore blocking resistance (Rf), and the concentration polarization resistance (Rp) was weak. The treatment efficiency of ultrafiltration membrane, and the differerce permeate flux on filtrate time and transmembrane pressure were investigated . When the transmembrane pressure was 0.1-0.5MPa, the average removal rates of COD and turbidity were 26.5% and 77.7%, respectively. SEM-EDX analysis results revealed that there were a large number of particulate matter and crystalline substances in the film surface, and Na, Ca, Cl, and S were the main inorganic elements. Finally, five different types of chemical cleaning reagents: pure water, HCl , NaOH, NaClO,and EDTA solutions, respectively,were used to clean the fouled membrane. Then the composition of eluants, the morphology of fouled membrane and cleaning membrane were analyzed.The results showed that 0.1mol/L HCl had better removal effect on inorganic metal ions, while 0.1mol/LNaOH had better removal effect on organic compounds, especially for humic acids and aromatic compounds.
桂双林(1984—),男,湖南永州,副研究员,博士研究生,研究方向:膜法水处理技术研究,E-mail:gsl503@163.com

参考文献:
[1]Yin S, Chen K, Srinivasakannan C, et al. Enhancing recovery of ammonia from rare earth wastewater by air stripping combination of microwave heating and high gravity technology[J]. Chem.Eng. J. 2018, (337): 515-521.
[2]Zeng G S, Ling B, Li Z J, et al. Fluorine removal and calcium fluoride recovery from rare-earth smelting wastewater using fluidized bed crystallization process[J]. Journal of Hazardous Materials, 2019, (373) :313–320
[3]桂双林, 麦兆环, 敖子强,等.南方稀土冶炼废水的特点及其处理技术研究进展[J].环境科学与管理, 2017, 42(7): 80-84.
[4] Malaeb L, Ayoub G M. Reverse osmosis technology for water treatment: State of the art review[J]. Desalination, 2011, (267): 1-8.
[5] Qasim M, Badrelzaman M, Darwish N N, et al. Reverse osmosis desalination: A state-of-the-art review[J]. Desalination, 2019, (459) :59–104
[6]黄海明, 晏波, 陈启华,等.稀土废水中高浓度氨氮处理与回收试验研究[J].环境工程学报, 2008, 2(5):652-655.
[7]胡亚芹, 吴春金, 叶向群,等.膜集成技术浓缩稀土废水中的氯化铵[J].水处理技术, 2005, 31(8): 38-39.
[8]Zhang L N, Xu B H, Gong J D, et al. Membrane combination technic on treatment and reuse of high ammonia and salts wastewater in rare earth manufacture process[J]. Rare Earths, 2010,28: 501-503.
[9] Kavitha J, Rajalakshmi M, Phani A R, et al. Pretreatment processes for seawater reverse osmosis desalination systems—A review[J]. Journal of Water Process Engineering, 2019 ,32: 100926
[10] Gu H, Rahardianto A, Gao L X, et al. Fouling indicators for field monitoring the effectiveness of operational strategies of ultrafiltration as pretreatment for seawater desalination[J]. Desalination , 2018 ,431:86–99
[11]Mai Z H, Gui S L, Fu J Q, et al. Activity-derived model for water and salt transport in reverse osmosismembranes: A combination of film theory and electrolyte theory[J]. Desalination 2019,469:114094
[12]Jermann D, Pronk W, Meylan S, et al. Interplay of different NOM fouling mechanisms during ultrafiltration for drinking water production[J]. Water Research, 2007,41(8):1713-1722.
[13]田岳林, 袁栋栋, 李汝琪. 陶瓷膜污染过程分析与膜清洗方法优化[J]. 环境工程学报, 2013,7(1):253-257
[14]孟晓荣,张海珍,王磊,等.城市污水二级出水超滤膜污染与膜特性的研究[J]. 环境科学,2013,34(5):1822-1827
[15]崔彦杰, 刘美, 王湛,等. 超滤通量模型的研究进展[J]. 膜科学与技术, 2008,28(6):93-98
[16]刘为, 曾作祥, 薛为岚,等. 错流超滤膜污染模型[J]. 华东理工大学学报(自然科学版), 2005,35(10): 589-592
[17]钱晓荣,戴勇.MF-UF组合工艺处理再生纸废水的实验研究[J]. 环境工程学报,2009,3(11): 2013-2016
[18]王歌,李方, 吴亮, 等. 聚乙烯醇(PVA)对模拟胞外聚合物(EPS)在错流超滤中膜污染的影响[J] .过程工程学报, 2012,12(3): 409-414
[19]闫欢汐, 许振钰, 金春姬,等.厌氧膜生物反应器处理含盐废水运行效能及膜污染特性[J]. 环境科学, 2019, 40(6): 2793-2799
[20]Ishizaki S, Fukushima T, Ishii S, et al. Membrane fouling potentials and cellular properties of bacteria isolated from fouled membranes in a MBR treating municipal wastewater[J].Water Research, 2016, 100: 448-457.
[21]Tang F, Hu H Y, Sun L J, et al. Fouling characteristics of reverse osmosis membranes at different positions of a full-scale plant for municipal wastewater reclamation[J]. Water Research, 2016, 90: 329-336.
[22]Espinasse B P, Chae S, Marconnet C, et al. Comparison of chemical cleaning reagentsand characterization of foulants of nanofiltration membranes used in surface water treatment[J].Desalination, 2012,296:1~6.
[23]Chon K, Cho J, Shon HK, et al. Advanced characterization of organic foulants of ultrafiltration and reverse osmosis from water reclamation[J]. Desalination, 2012,301:59~66.

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