1. 南开大学环境科学与工程学院,天津,300071
2. 西安交通大学能源与动力工程学院,西安,710049
网络首发:2012-05-10,
纸质出版:2012
移动端阅览
王玉珍 1, 2, 王建友 1, 等. 工艺参数对电去离子技术浓缩分离含镍离子溶液的影响[J]. 西安交通大学学报, 2012,46(5):114-119.
Influences of Operation Parameters on Concentration and Separation of Nickel-Containing Solution by Electrodeionization Process[J]. 2012, 46(5): 114-119.
采用浓缩室填充树脂的强化电去离子(EDI)对含Ni
2+
溶液进行了浓缩分离
从中研究了工作电压、淡化室隔板厚度、原水浓度及组分对EDI分离性能的影响.结果表明
在15 V电压下
EDI以增强传质模式运行可在较低能耗下获得高质量的出水; 电压增大使淡水室内发生水解离而产生结垢
影响EDI的稳定运行.淡化室隔板由3 mm增至5 mm时
膜堆电阻增大
分离效率降低.对于含Ni
2+
为50 mg·L
-1
的NiSO
4
原水
在优化条件下
浓、淡水出水中Ni
2+
浓度分别为11 031和2.78 mg·L
-1
Ni
2+
的浓缩倍数达223.对于含Ni
2+
和Cu
2+
各25 mg·L
-1
的双组分原水
EDI对Cu
2+
有更好的浓缩效果.实验结束时
浓水出水中Ni
2+
、Cu
2+
浓度分别为3 258和4 690 mg·L
-1
浓缩倍数分别为130和187; 淡水出水中Ni
2+
及Cu
2+
浓度分别为4.71和3.71 mg·L
-1
.
The enhanced electrodeionization(EDI)in the dilute and concentrate chambers filled with ion exchanges resins was adopted for the concentration and separation of nickel-containing solution. The influences of operation voltage
partition thickness of the dilute chamber
feed concentration and composition on separation performance were examined. The results show that the EDI process operating under the enhanced mass transfer mode at applied stack voltage of 15V could ensure high quality effluent with lower energy consumption. As the voltage increased
significant water decomposition occurred in the dilute compartments
resulting in scaling problem and unstable operation. When the partition thickness of dilute chambers increased from 3mm to 5mm
the separation performance of the EDI process decreased as the stack resistance increased. Under the optimized conditions
for the Ni
2+
feed concentration of 50 mg·L
-1
the Ni
2+
concentration of the outlet concentrate and dilute was 11 131 and 2.78 mg·L
-1
respectively
i.e.
the concentration ratio of higher than 223. However
when the feed solution contained Ni
2+
and Cu
2+
with the same concentration of 25 mg·L
-1
the concentration effect of Cu
2+
was better than that of Ni
2+
. At the end of the experiment
the concentration of Ni
2+
and Cu
2+
in the concentrate effluent was 3 258 and 4 690mg·L
-1
while that in the dilute effluent was 4.71 and 3.71 mg·L
-1
respectively.
XING Yunqing, CHEN Xueming. Variable effects on the performance of continuous electrodeionization for the removal of Cr(Ⅵ)from wastewater [J]. Separation and Purification Technology, 2009, 68(3): 357-362.
XIAO Feng, GAO Junsong, WU Zucheng. Removal of copper ions from electroplating rinse water using eletrodeionization [J]. Journal of Zhejiang University: Science A, 2008, 9A(9): 1283-1287.
TAGHDIRIAN H R, MOHEB A, MEHDIPOUR-GHAZI M. Selective separation of Ni(Ⅱ)/Co(Ⅱ)ions from dilute aqueous solutions using continuous electrodeionization in the presence of EDTA[J]. Journal of Membrane Science, 2010, 362(1/2): 68-75.
王玉珍, 王建友, 卢会霞, 等. 电去离子集成过程分级浓缩与纯化电镀镍漂洗废水[J]. 化工学报, 2010, 61(3): 754-760.
WANG Yuzhen, WANG Jianyou, LU Huixia, et al. Successive concentrating and purifying nickel electroplating rinsing wastewater by integrated membrane processes with electrodeionization [J]. CIESC Journal, 2010, 61(3): 754-760.
LU Huixia, WANG Jianyou, YAN bo, et al. Recovery of nickel ions from simulated electroplating rinse water by electrodeionization process [J]. Water Science and Technology, 2010, 61(3): 729-735.
任安娟, 王建友, 卢会霞, 等. 电去离子技术同步纯化和浓缩含镍离子溶液的研究 [J]. 现代化工, 2009, 29(6): 55-60.
REN Anjuan, WANG Jianyou, LU Huixia, et al. Study on purifying and concentrating nickel wastewater synchronously by EDI [J]. Modern Chemical Industry, 2009, 29(6): 55-60.
王玉珍, 王建友, 卢会霞, 等. 倒极电去离子(EDI)过程浓缩分离含镍离子溶液[J]. 化工学报, 2010, 6(10): 2688-2693.
WANG Yuzhen, WANG Jianyou, LU Huixia, et al. Concentration and separation of nickel-containing solution by electrodeionization with polarity reversal[J]. CIESC Journal, 2010, 6(10):2688-2693.
王建友. 电去离子过程的传质机理及其集成膜过程的研究 [D]. 天津: 天津大学, 2002.
钱庭宝. 离子交换剂应用技术 [M]. 天津: 天津科学技术出版社, 1984: 77-78.
HELFFERICH F G. Ion exchange [M]. New York,USA: McGraw Hill Book Company, 1962: 250-322.
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