Removal of Cd(II) ions from aqueous solution and industrial effluent using reverse osmosis and nanofiltration membranes

被引:59
作者
Kheriji, Jamel [1 ]
Tabassi, Dorra [1 ]
Hamrouni, Bechir [1 ]
机构
[1] Tunis El Manar Univ, Desalinat & Water Treatment Res Unit, Fac Sci Tunis, El Manar 2092 2, Tunisia
关键词
aqueous effluent; cadmium; NF/RO; Spiegler-Kedem model; TRANSPORT PARAMETERS; OPERATING-CONDITIONS; SURFACE-CHARGE; RO MEMBRANES; HEAVY-METALS; WASTE-WATER; KEDEM MODEL; REJECTION; CADMIUM; NF;
D O I
10.2166/wst.2015.326
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Industrial effluents loaded with cadmium have contributed to the pollution of the environment and health troubles for humans. Therefore, these effluents need treatment to reduce cadmium concentration before releasing them to public sewage. The purpose of the research is to study the major role of reverse osmosis (RO) and nanofiltration (NF) processes, which can contribute to the removal of cadmium ions from model water and wastewater from the battery industry. For this reason, two RO and two nanofiltration membranes have been used. The effects of feed pressure, concentration, ionic strength, nature of anion associated with cadmium and pH on the retention of Cd(II) were studied with model solutions. Thereafter, NF and RO membranes were used to reduce cadmium ions and total salinity of battery industry effluent. Among these membranes, there are only three which eliminate more than 95% of cadmium. This was found to depend on operating conditions. It is worth noting that the Spiegler-Kedem model was applied to fit the experimental results.
引用
收藏
页码:1206 / 1216
页数:11
相关论文
共 28 条
  • [1] Reverse osmosis brine staging treatment of subsurface water
    Al-Wazzan, Y
    Safar, M
    Mesri, A
    [J]. DESALINATION, 2003, 155 (02) : 141 - 151
  • [2] Savings and re-use of salts and water present in dye house effluents
    Allègre, C
    Moulin, P
    Maisseu, M
    Charbit, F
    [J]. DESALINATION, 2004, 162 (1-3) : 13 - 22
  • [3] Transport coefficients cadmium salt rejection in nanofiltration membrane
    Ballet, GT
    Gzara, L
    Hafiane, A
    Dhahbi, M
    [J]. DESALINATION, 2004, 167 (1-3) : 369 - 376
  • [4] The role of membrane surface charge and solute physico-chemical properties in the rejection of organic acids by NF membranes
    Bellona, C
    Drewes, JE
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2005, 249 (1-2) : 227 - 234
  • [5] Influence of the operating conditions on the elimination of zinc ions by nanofiltration
    Ben Frarès, N
    Taha, S
    Dorange, G
    [J]. DESALINATION, 2005, 185 (1-3) : 245 - 253
  • [6] NITROGEN SEPARATION FROM DOMESTIC WASTE-WATER BY REVERSE-OSMOSIS
    BILSTAD, T
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1995, 102 : 93 - 102
  • [7] Effect of solution chemistry on the surface charge of polymeric reverse osmosis and nanofiltration membranes
    Childress, AE
    Elimelech, M
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1996, 119 (02) : 253 - 268
  • [8] Zeta potential of commercial RO membranes: influence of source water type and chemistry
    Deshmukh, SS
    Childress, AE
    [J]. DESALINATION, 2001, 140 (01) : 87 - 95
  • [9] Essington M.E., 2004, Soil and Water Chemistry: An Integrated Approach
  • [10] High organic content industrial wastewater treatment by membrane filtration
    Galambos, L
    Molina, JM
    Járay, P
    Vatai, G
    Bekássy-Molnár, E
    [J]. DESALINATION, 2004, 162 (1-3) : 117 - 120