期刊文献+

Coking wastewater treatment for industrial reuse purpose: Combining biological processes with ultrafiltration, nanofiltration and reverse osmosis 被引量:39

Coking wastewater treatment for industrial reuse purpose: Combining biological processes with ultrafiltration, nanofiltration and reverse osmosis
原文传递
导出
摘要 A full-scale plant using anaerobic, anoxic and oxic processes (A1/A2/O), along with a pilot-scale membrane bioreactor (MBR), nanofiltration (NF) and reverse osmosis (RO) integrated system developed by Shanghai Baosteel Chemical Co. Ltd., was investigated to treat coking wastewater for industrial reuse over a period of one year. The removals reached 82.5% (COD), 89.6% (BOD), 99.8% (ammonium nitrogen), 99.9% (phenol), 44.6% (total cyanide (T-CN)), 99.7% (thiocyanide (SCN-)) and 8.9% (fluoride), during the A1/A2/O biological treatment stage, and all parameters were further reduced by over 96.0%, except for fluoride (86.4%), in the final discharge effluent from the currently operating plant. The pilot-scale MBR process reduced the turbidity to less than 0.65 NTU, and most of the toxic organic compounds were degraded or intercepted by the A1/A2/O followed MBR processes. In addition, parameters including COD, T-CN, total nitrogen, fluoride, chloride ion, hardness and conductivity were significantly reduced by the NF-RO system to a level suitable for industrial reuse, with a total water production ratio of 70.7%. However, the concentrates from the NF and RO units were highly polluted and should be disposed of properly or further treated before being discharged. A full-scale plant using anaerobic, anoxic and oxic processes (A1/A2/O), along with a pilot-scale membrane bioreactor (MBR), nanofiltration (NF) and reverse osmosis (RO) integrated system developed by Shanghai Baosteel Chemical Co. Ltd., was investigated to treat coking wastewater for industrial reuse over a period of one year. The removals reached 82.5% (COD), 89.6% (BOD), 99.8% (ammonium nitrogen), 99.9% (phenol), 44.6% (total cyanide (T-CN)), 99.7% (thiocyanide (SCN-)) and 8.9% (fluoride), during the A1/A2/O biological treatment stage, and all parameters were further reduced by over 96.0%, except for fluoride (86.4%), in the final discharge effluent from the currently operating plant. The pilot-scale MBR process reduced the turbidity to less than 0.65 NTU, and most of the toxic organic compounds were degraded or intercepted by the A1/A2/O followed MBR processes. In addition, parameters including COD, T-CN, total nitrogen, fluoride, chloride ion, hardness and conductivity were significantly reduced by the NF-RO system to a level suitable for industrial reuse, with a total water production ratio of 70.7%. However, the concentrates from the NF and RO units were highly polluted and should be disposed of properly or further treated before being discharged.
出处 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2013年第8期1565-1574,共10页 环境科学学报(英文版)
关键词 coking wastewater industrial water reuse biological treatment MBR NF-RO coking wastewater industrial water reuse biological treatment MBR NF-RO
  • 相关文献

参考文献1

二级参考文献22

  • 1Chen F G,1994.The A/O process of the Xucheng coke plant[J].Water Supply and Discharge,1:17-30.
  • 2Christine Helmer,Sabine Kunst,1998.Simultaneous nitrification/denitrification in an aerobic biofilm system[J].Wat Sci Tech,37(4/5):183-187.
  • 3Grady C P,1990.Biodegradation of toxic organics:status and potential[J].Environ Eng,116 (5):805-819.
  • 4Hong W Z,Donald S M,Willian K O et al.,1999.Controlling factors for simultaneous nitrification and denitrification in a two-stage intermittent aeration process treating domestic sewage[J].Water Res,33(4):961-970.
  • 5Hyungseok Y,1999.Nitrogen removal from synthetic wastewater by simultaneous nitrification and denitrification (SND) via nitrite in a intermittently-aerated reactor[J].Water Res,33(1):145-154.
  • 6Jiang W H,1993.Study on the treatment of coke plant wastewater by biological rotator[J].Industrial Wastewater Treatment,13(4):18-20.
  • 7Kong Q X,Li J Y,2004.The progress on biological nitrogen removal via aerobic denitrification[J].Environment and Health,21(3):189-191.
  • 8Li C J,Geng Y,Zhou Q et al.,2001.SMSBR characters in removing the organic matter and nitrogen in coke plant wastewater[J].Water Supply and Drainage in China,17(5):6-11.
  • 9Li Y M,1999.Study on biological treatment process and mechanism for toxic and refractory organic wastewater (coke plant wastewater)[D].Shanghai:Tongji University.
  • 10Luthy R G,Stamoudis V C,Campbell J R et al.,1983.Removal of organic contaminants from coal conversion process condensates[J].Water Pollut Control Fed,55(3):196-207.

共引文献32

同被引文献404

引证文献39

二级引证文献249

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部