响应面法优化UV/H2O2光氧化法处理高浓度LAS废水

曹先仲, 魏未, 朱丽娟. 响应面法优化UV/H2O2光氧化法处理高浓度LAS废水[J]. 环境工程学报, 2014, 8(4): 1543-1548.
引用本文: 曹先仲, 魏未, 朱丽娟. 响应面法优化UV/H2O2光氧化法处理高浓度LAS废水[J]. 环境工程学报, 2014, 8(4): 1543-1548.
Cao Xianzhong, Wei Wei, Zhu Lijuan. Optimization of UV/H2O2 photo oxidation process to treat high concentration LAS wastewater by response surface methodology[J]. Chinese Journal of Environmental Engineering, 2014, 8(4): 1543-1548.
Citation: Cao Xianzhong, Wei Wei, Zhu Lijuan. Optimization of UV/H2O2 photo oxidation process to treat high concentration LAS wastewater by response surface methodology[J]. Chinese Journal of Environmental Engineering, 2014, 8(4): 1543-1548.

响应面法优化UV/H2O2光氧化法处理高浓度LAS废水

  • 基金项目:
  • 中图分类号: X703.1

Optimization of UV/H2O2 photo oxidation process to treat high concentration LAS wastewater by response surface methodology

  • Fund Project:
  • 摘要: 采用响应面法对UV/H2O2光氧化法处理高浓度LAS废水的工艺参数进行了系统研究。根据Box-Behnken Design(BBD)设计原理,以初始pH与H2O2投加量、反应时间和温度为主要影响因素,设计4因素3水平共29个实验点的实验方案,并建立了二次响应面拟合模型。方差分析表明,初始pH与H2O2投加量、反应时间和温度以及初始pH和H2O2投加量、H2O2投加量和温度之间的交互作用,对实验结果具有显著性影响。实验得到的光氧化高浓度LAS废水最佳工艺条件,pH为4.0,H2O2投加量为40 mmol/L,反应时间为90 min,温度为25℃,在此条件下,LAS的平均去除率为98.1%。
  • 加载中
  • [1] 蒋永生, 高宇.超声波降解废水中十二烷基苯磺酸钠的实验研究.重庆工商大学学报(自然科学版), 2004, 21 (1):32-34 Jiang Y.S., Gao Y.Decomposition of sodium dodecylneopelex in wastewater by using ultrasonic wave.Journal of CTBU (Nat.Scien.Edit.), 2004, 21 (1):32-34(in Chinese)
    [2] Khleifat K.M.Biodegradation of linear alkylbenzene sulphonate by a two member facultative anaerobic bacterial consortium.Enzyme Microb.Tech., 2006, 39(5):1030-1035
    [3] Jensen J.Fate and effects of linear alkylbenzene sulphonate (LAS) in the terrestrial environment.Sci.of the Total Environ., 1999, 226(2):93-111
    [4] Visarut R., Triroj M., Orathai P., et al.Recovery of surfactant from an aqueous solution using continuous multistage foam fractionation:Mixed surfactant system.Sep.Sci.Technol., 2013, 48 (5):757-765
    [5] Yang W.B., Xia M.F., Li A., M., et al.Mechanism and behavior of surfactant adsorption onto resins with different matrices.React Funct Polym, 2007, 67 (7):609-616
    [6] Beltran-Heredia J., Sanchez-Martin J.Removal of sodium lauryl sulphate by coagulation/flocculation with Moringa oleifera seed extract.J.Hazard.Mater., 2009, 164 (2-3):713-719
    [7] 高建峰, 徐春彦, 白婷婷.用CuO/AC催化氧化降解水中 LAS的研究.工业水处理, 2008, 28 (6):47-50 Gao J F., Xu C Y., Bai T.T.Research on the catalytic oxidation degradation of aqueous LAS by using CuO/AC.Industrial Water Treatment, 2008, 28 (6):47-50(in Chinese)
    [8] Cao X Z., Li Y M.Treatment of linear alkylbenzene sulfonate (LAS) wastewater by internal electrolysis-biological contact oxidation process.Water Sci.and Technol.2011, 64 (1):147-154
    [9] Khaled M., Khleifat.Biodegradation of linear alkybenzene sulfonate by a two-member facultative an aerobic bacterial consortium.Enzyme Microb.Tech., 2006, 36:1030-1035
    [10] Oliveira L L., Costa R B., Okada D.B., et al.Anaerobic degradation of linear alkylbenzene sulfonate (LAS) in fluidized bed reactor by microbial consortia in different support materials.Bioresource Technol., 2010, 101 (14):5112-5122
    [11] Bazri M M., Barbeau B., Mohseni M.Impact of UV/H2O2 advanced oxidation treatment on molecular weight distribution of NOM and biostability of water.Water Res., 2012, 46 (16):5297-5304
    [12] Bounty S., Rodriguez R.A., Linden K.G.Inactivation of adenovirus using low-dose UV/H2O2 advanced oxidation.Water Res., 2012, 46 (19):6173-6278
    [13] 潘晶, 孙铁珩, 李海波.水中无机阴离子对UV/H2O2降解LAS 的影响及机理.环境科学, 2007, 28 (11):2539-2543 Pan J., Sun T H., Li H B.Effects and mechanisms of inorganic anions in water on degradation of LAS by UV/H2O2 combination process.Environmental Science, 2007, 28 (11):2539-2543(in Chinese)
    [14] Sanz J., Lombraña J I., de Luis A.Temperature-assisted UV/H2O2 oxidation of concentrated linear alkylbenzene sulphonate (LAS) solutions.Chem.Eng.J., 2013, 215-216:533-541
    [15] Li Q.S., Gao N.Y., Deng Y., et al.Factors affecting UV/H2O2 oxidation of 17 alpha-ethynyestradiol in water.Clean-soil Air Water, 2013, 41 (2):143-147
    [16] Faki D., Ojstrsek A.Optimization of removal of colour and organic pollutants from textile wastewater treated with UV/H2O2 adopting the Plackett-Burman factorial design.Desalin Water Treatment, 2013, 51 (7-9):1584-1589
    [17] Rand M.C., Greenberg A.E., Taras M.J.Standard Methods for the Examination of Water and Wastewater(14th ed.).Prepared and published jointly by American Public Health Association, American Water Works Association, and Water Pollution Control Federation, 1976
  • 加载中
计量
  • 文章访问数:  1885
  • HTML全文浏览数:  1128
  • PDF下载数:  1279
  • 施引文献:  0
出版历程
  • 收稿日期:  2013-04-18
  • 刊出日期:  2014-03-28
曹先仲, 魏未, 朱丽娟. 响应面法优化UV/H2O2光氧化法处理高浓度LAS废水[J]. 环境工程学报, 2014, 8(4): 1543-1548.
引用本文: 曹先仲, 魏未, 朱丽娟. 响应面法优化UV/H2O2光氧化法处理高浓度LAS废水[J]. 环境工程学报, 2014, 8(4): 1543-1548.
Cao Xianzhong, Wei Wei, Zhu Lijuan. Optimization of UV/H2O2 photo oxidation process to treat high concentration LAS wastewater by response surface methodology[J]. Chinese Journal of Environmental Engineering, 2014, 8(4): 1543-1548.
Citation: Cao Xianzhong, Wei Wei, Zhu Lijuan. Optimization of UV/H2O2 photo oxidation process to treat high concentration LAS wastewater by response surface methodology[J]. Chinese Journal of Environmental Engineering, 2014, 8(4): 1543-1548.

响应面法优化UV/H2O2光氧化法处理高浓度LAS废水

  • 1.  河南省冶金研究所有限责任公司, 郑州 450053
  • 2.  河南省科学院质量检验与分析测试研究中心, 郑州 450008
基金项目:

摘要: 采用响应面法对UV/H2O2光氧化法处理高浓度LAS废水的工艺参数进行了系统研究。根据Box-Behnken Design(BBD)设计原理,以初始pH与H2O2投加量、反应时间和温度为主要影响因素,设计4因素3水平共29个实验点的实验方案,并建立了二次响应面拟合模型。方差分析表明,初始pH与H2O2投加量、反应时间和温度以及初始pH和H2O2投加量、H2O2投加量和温度之间的交互作用,对实验结果具有显著性影响。实验得到的光氧化高浓度LAS废水最佳工艺条件,pH为4.0,H2O2投加量为40 mmol/L,反应时间为90 min,温度为25℃,在此条件下,LAS的平均去除率为98.1%。

English Abstract

参考文献 (17)

返回顶部

目录

/

返回文章
返回