2012 Volume 6 Issue 11
Article Contents

Wang Qi, Lü Yongkang, Zhang Rong, Bi Jicheng. Supercritical water oxidation of cotton textiles dyeing wastewater[J]. Chinese Journal of Environmental Engineering, 2012, 6(11): 3959-3964.
Citation: Wang Qi, Lü Yongkang, Zhang Rong, Bi Jicheng. Supercritical water oxidation of cotton textiles dyeing wastewater[J]. Chinese Journal of Environmental Engineering, 2012, 6(11): 3959-3964.

Supercritical water oxidation of cotton textiles dyeing wastewater

  • Received Date: 14/10/2011
    Accepted Date: 16/09/2011
    Available Online: 09/11/2012
    Fund Project:
  • Cotton textiles dyeing wastewater was treated by supercritical water oxidation (SCWO) in a continuous flow tubular reactor using hydrogen peroxide (H2O2) as an oxidant. The degradation of total organic carbon(TOC)and the ammonia and nitrogen(NH3-N)were studied at the temperature range of 400~600℃,25 MPa,residence time bewteen 10~45 s and excess oxygen varying from 0%~400%. The results showed that temperature is the most important factor influencing TOC degradation. The TOC degradation efficiency varies with excess oxygen at different temperatures. At 450℃, 20 s and excess O2 300%, the degradation efficiency of TOC is 98.94%. The degradation of NH3-N is closely related to temperature and excess oxygen of the reaction. When excess oxygen of 300%, the NH3-N concentration decreases from 55.42 mg/L to 3.31 mg/L as the temperature increases from 400℃ to 600℃. When oxidizing agent is absent at 600℃, the degradation of NH3 is difficult. The effects of excess oxygen and residence time of the reaction on the NH3 degradation are not obvious at 450℃.
  • 加载中
  • [1] 朱虹,孙杰. 印染废水处理技术. 北京:中国纺织出版社,2004.189-215

    Google Scholar Pub Med

    [2] 杨书铭,黄长盾.纺织印染工业废水治理技术. 北京:化学工业出版社,2002.30-36

    Google Scholar Pub Med

    [3] Robinson T., McMullan G., Marchant R., et al. Remediation of dyes in textile effluent: A critical review on current treatment technologies with a proposed alternative. Bioresource Technology,2001, 77(3): 247-255

    Google Scholar Pub Med

    [4] Söüt Onur Ö., Akgün M. Treatment of dyehouse waste-water by supercritical water oxidation: A case study. Journal of Chemical Technology and Biotechnology, 2010, 85(5):640-647

    Google Scholar Pub Med

    [5] Ciardelli G., Ranieri N. The treatment and reuse of wastewater in the textile industry by means of ozonation and electroflocculation. Water Research, 2001, 35(2): 567-572

    Google Scholar Pub Med

    [6] Chen G. Electrochemical technologies in wastewater treatment. Separation and Purification Technology, 2004, 38(1): 11-41

    Google Scholar Pub Med

    [7] Ciardelli G., Corsi L., Marcucci M. Membrane separation for wastewater reuse in the textile industry. Resources, Conservation and Recycling, 2001, 31(2): 189-197

    Google Scholar Pub Med

    [8] Lee D.K., Cho I.C., Lee G.S. Catalytic wet oxidation of reactive dyes with H2/O2 mixture on Pd-Pt/Al2O3 catalysts. Separation and Purification Technology, 2004, 34(3): 43-50

    Google Scholar Pub Med

    [9] 周文俊,钱仁渊.催化湿式氧化法处理含酚废水.南京工业大学学报,2004, 26(1): 63-67 Zhou Wenjun, Qian Renyuan. Catalytic wet oxidation of phenolic wastewater. Journal of Nanjing University of Technology, 2004, 26(1): 63-67 (in Chinese)

    Google Scholar Pub Med

    [10] Veriansyah B., Kim J.D. Supercritical water oxidation for the destruction of toxic organic wastewaters: A review. Journal of Environmental Sciences, 2007, 19(5): 513-522

    Google Scholar Pub Med

    [11] Shin Y.H., Shin N.C., Veriansyah B., et al. Supercritical water oxidation of wastewater from acrylonitrile manufacturing plant. Journal of Hazard. Mater., 2009, 163(2):1142-1147

    Google Scholar Pub Med

    [12] Gong W., Li F., Xi D.L. Oxidation of industrial dyeing wastewater by supercritical water oxidation in transpiring-wall reactor. Water Environment Research, 2008, 80(2):186-192

    Google Scholar Pub Med

    [13] Söüt Onur Ö., Akgün M. Removal of C.I. Basic Blue 41 from aqueous solution by supercritical water oxidation in continuous-flow reactor. Journal of Industrial and Engineering Chemistry, 2009, 15(6): 803-808

    Google Scholar Pub Med

    [14] Söüt Onur Ö., Akgün M. Treatment of textile wastewater by SCWO in a tube reactor. Journal of Supercritical Fluids, 2007, 43(1): 106-111

    Google Scholar Pub Med

    [15] Harvey A.H., Peskin A.P., Klein S.A. NIST/ASME Steam Properties, NIST Standard Reference Database 10, Version 2.2. Gaithersburg, MD: National Institute of Standard and Technology, 2000

    Google Scholar Pub Med

    [16] Du X., Zhang R., Gan Z., et al. Treatment of high strength coking wastewater by supercritical water oxidation. Fuel, 2010, doi:10.1016/j.fuel.2010.09.018

    Google Scholar Pub Med

    [17] Segond N., Matsumura Y., Yamamoto K. Determination of ammonia oxidation rate in sub-and supercritical water. Industrial & Engineering Chemistry Research, 2002, 41(24): 6020-6027

    Google Scholar Pub Med

    [18] Al-Duri B., Pinto L., Ashraf-Ball N.H. Thermal abatement of nitrogen-containing hydrocarbons by non-catalytic supercritical water oxidation (SCWO). Journal of Materials Science, 2008, 43(4):1421-1428

    Google Scholar Pub Med

    [19] 马春燕.印染废水深度处理及回用技术研究. 上海: 东华大学博士学位论文,2007. 29-32 Ma Chunyan. Study on advanced treatment and reuse technology of printing and dyeing wastewater. Shanghai: Doctor Dissertation of Donghua University,2007. 29-32(in Chinese)

    Google Scholar Pub Med

  • 加载中
通讯作者: 陈斌, bchen63@163.com
  • 1. 

    沈阳化工大学材料科学与工程学院 沈阳 110142

  1. 本站搜索
  2. 百度学术搜索
  3. 万方数据库搜索
  4. CNKI搜索

Article Metrics

Article views(2249) PDF downloads(1946) Cited by(0)

Access History

Supercritical water oxidation of cotton textiles dyeing wastewater

Fund Project:

Abstract: Cotton textiles dyeing wastewater was treated by supercritical water oxidation (SCWO) in a continuous flow tubular reactor using hydrogen peroxide (H2O2) as an oxidant. The degradation of total organic carbon(TOC)and the ammonia and nitrogen(NH3-N)were studied at the temperature range of 400~600℃,25 MPa,residence time bewteen 10~45 s and excess oxygen varying from 0%~400%. The results showed that temperature is the most important factor influencing TOC degradation. The TOC degradation efficiency varies with excess oxygen at different temperatures. At 450℃, 20 s and excess O2 300%, the degradation efficiency of TOC is 98.94%. The degradation of NH3-N is closely related to temperature and excess oxygen of the reaction. When excess oxygen of 300%, the NH3-N concentration decreases from 55.42 mg/L to 3.31 mg/L as the temperature increases from 400℃ to 600℃. When oxidizing agent is absent at 600℃, the degradation of NH3 is difficult. The effects of excess oxygen and residence time of the reaction on the NH3 degradation are not obvious at 450℃.

Reference (19)

Catalog

    /

    DownLoad:  Full-Size Img  PowerPoint