| 催化铁内电解法处理制革综合废水的研究 |
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| 引用本文： | 卢亮,肖华.催化铁内电解法处理制革综合废水的研究[J].污染防治技术,2006,19(2):16-17,53. |
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| 作者姓名： | 卢亮 肖华 |
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| 作者单位： | [1]河北工程大学城市建设学院,河北邯郸056038 [2]中国科学院生态环境研究中心,北京100085 |
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| 摘 要： | 采用以催化铁内电解法为主的工艺处理制革综合废水，当进水SS、BOD5、CODCr、TCr、S^2-、色度分别为2120mg／L、648mg／L、1240mg／L、96．2mg／L、113．8mg／L、840倍时，出水分别为142mg／L、75mg／L、248mg／L、1．3mg／L、0．8mg／L、16倍，而且出水水质稳定，能够达到二级排放标准。
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| 关 键 词： | 催化铁内电解 制革综合废水 预曝气调节池 絮凝沉淀 |
| 收稿时间： | 2005-10-21 |
| 修稿时间： | 2005-10-21 |
Research of Synthetical Tan Wastewater Treatment with Catalyzed Iron Internal Electrolysis |
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| LU Liang, XIAO Hua.Research of Synthetical Tan Wastewater Treatment with Catalyzed Iron Internal Electrolysis[J].Pollution Control Technology,2006,19(2):16-17,53. |
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| Authors: | LU Liang XIAO Hua |
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| Abstract: | Adopting the technology with Catalyzed Iron Internal Electrolysis giving priority to handle the Synthetical Tan Wastewater, when the intake water appear that the SS, BOD5 , CODCr, chromium invariably, S2- and chrominance separately in the interest of 2 120 mg/L, 1 240 mg/L, 96.2 mg/L, 113.8 mg/L and 840 - fold, the indication of outlet water is 142 mg/L and 75 mg/L and 248 mg/L and 1.3 mg/L and 0.8 mg/L and 16 - fold, and the water quality can steadily meet the second class of dischange standards. This technology operation is portabe, and the cost is inexpensive. |
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| Keywords: | Catalyzed Iron internal electrolysis synthctical tan wastewater beforehand gas regulate pool flocculate precipitation |
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