A one-step electrochlorination/electroflotation process for the treatment of heavy metals wastewater in presence of EDTA

被引:42
|
作者
Khelifa, A. [1 ]
Aoudj, S. [1 ,2 ]
Mallay, S. [3 ]
De Petris-Weryd, M. [4 ]
机构
[1] Univ Saad Dahlab Blida, Lab Genie Chim, Dept Chim Ind, Fac Sci Ingn, Blida 09000, Algeria
[2] CRTSE, Algiers 16038, Algeria
[3] Univ Sadd Dahlab Blida, Lab Chim Phys Mol & Macromol, Dept Chim Ind, Fac Sci Ingn, Blida 09000, Algeria
[4] IUT Dept Mesures Phys Orsay, F-91400 Orsay, France
关键词
Metal finishing industry; Heavy metals; EDTA; Ti/RuO2; anode; Electroflotation; Electrochlorination; ELECTROFLOTATION; CHLORINE; OXIDATION; PERFORMANCE; IONS;
D O I
10.1016/j.cep.2013.04.013
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This study demonstrated the feasibility of simultaneous removal of heavy metals and EDTA in an electrolytic undivided cell equipped with Ti/RuO2 as anode and stainless steel as cathode. In absence of EDTA, results show that nickel and copper removal by EF process is pH sensitive. In addition, nickel and copper may be substantially removed by EF. Removal efficiencies were 99.6% and 97%, respectively. In presence of EDTA, the metal removal by the EF process was inhibited. The inhibition rate was found to be dependent on EDTA/metal molar ratio. A one-step process, involving the combination of two techniques electrochlorination (EC) and electroflotation (EF), was set thanks to chloride addition. In situ generated active chlorine allowed the decomplexation of M-EDTA. Then, free metal ions were removed by precipitating and subsequent floating to the surface by rising electrogenerated bubbles. The obtained results revealed that, with 0.6 EDTA/metal molar ratio, removal efficiencies were 77% and 78% for nickel and EDTA, respectively, in the case of nickel EDTA solutions. Removal efficiencies were 89% and 96% for copper and EDTA, respectively, in the case of copper EDTA solutions. Furthermore, heavy metal removal efficiency by the combined process showed to be affected by chloride content and current intensity. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:110 / 116
页数:7
相关论文
共 50 条
  • [41] ASTIGMATIC ONE-STEP RAINBOW HOLOGRAM PROCESS
    CHEN, H
    APPLIED OPTICS, 1979, 18 (22) : 3728 - 3730
  • [42] One-step recovery of nickel by an electrohydrometallurgical process
    Page, P.W.
    Brandon, N.P.
    Mahmood, M.N.
    Fogarty, P.O.
    Journal of Applied Electrochemistry, 1992, 22 (09): : 779 - 786
  • [43] CONVERSION OF PEPSINOGEN INTO PEPSIN IS NOT A ONE-STEP PROCESS
    DYKES, CW
    KAY, J
    BIOCHEMICAL JOURNAL, 1976, 153 (01) : 141 - 144
  • [44] Converting lignin into plastics in one-step process
    不详
    INTERNATIONAL SUGAR JOURNAL, 2017, 119 (1427): : 862 - 862
  • [45] PROCESS INDUSTRIES TAKE ONE-STEP AT A TIME
    BLICKLEY, GJ
    CONTROL ENGINEERING, 1985, 32 (06) : 83 - 84
  • [46] Catalyst offers one-step amine process
    不详
    TCE, 2008, (805): : 17 - 17
  • [47] Oriented aluminum nanocrystals in a one-step process
    Veith, M.
    Grobelsek, I.
    Kirs, T.
    Aktas, C.
    Dufloux, C.
    THIN SOLID FILMS, 2014, 564 : 128 - 134
  • [48] Integrated Process of Immediate One-Step Lime Precipitation, Atmospheric Carbonation, Constructed Wetlands, or Adsorption for Industrial Wastewater Treatment: A Review
    Madeira, Luis
    Carvalho, Fatima
    Almeida, Adelaide
    Teixeira, Margarida Ribau
    WATER, 2023, 15 (22)
  • [49] ELECTROCAL ONE-STEP COLOUR TRANSFER PROCESS
    不详
    RUBBER AND PLASTICS AGE, 1969, 50 (03): : 206 - &
  • [50] ONE-STEP RECOVERY OF NICKEL BY AN ELECTROHYDROMETALLURGICAL PROCESS
    PAGE, PW
    BRANDON, NP
    MAHMOOD, MN
    FOGARTY, PO
    JOURNAL OF APPLIED ELECTROCHEMISTRY, 1992, 22 (09) : 779 - 786