Desalination of spent ion-exchange resin regeneration solutions by suspension freeze crystallization

被引:17
|
作者
Mountadar, S. [1 ,2 ]
Guessous, M. [2 ]
Rich, A. [2 ]
Karmil, F. Z. [1 ]
El Alaoui Belghiti, H. [3 ]
Siniti, M. [2 ]
Tahiri, S. [1 ]
机构
[1] Univ Chouaib Doukkali, Fac Sci, Dept Chem, Lab Water & Environm, POB 20, El Jadida 24000, Morocco
[2] Univ Chouaib Doukkali, Fac Sci, Dept Chem, Res Team Thermodynam Catalysis & Surfaces, POB 20, El Jadida 24000, Morocco
[3] Univ Chouaib Doukkali, Fac Sci, Dept Chem, Lab Phys Chem Mat, POB 20, El Jadida 24000, Morocco
关键词
Spent ion-exchange resin; Solutions from regeneration; Desalination; Suspension freeze crystallization; WATER; RECOVERY; SYSTEM;
D O I
10.1016/j.desal.2019.06.025
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The aim of this work is to evaluate the desalination of spent ion-exchange resin regeneration solutions by freeze suspension crystallization. The main steps used during freezing experiments are solution cooling followed by seeding to start the nucleation and then sweating in order to increase the purity of the obtained ice crystals. The study has shown that the purity of the ice crystals is highly dependent on the operating conditions. The obtained results have shown that seeding, an increase in stirring speed and a diminution in crystal growth rate lead to higher yields by decreasing the value of total dissolved solids (S-i) of ice crystals from 6.34 to 2.59 g/L without a significant effect on the recovered mass (from 220.97 to 202.23 g, respectively). Moreover, adding the sweating step at the end of the process has led to increase the ice purity by melting the impure areas until reaching an S-i value of about 0.63 g/L after 5 h of sweating (with a loss of mass of about 13.6%). The effect of the solution salinity was also evaluated and the results showed that freezing process performance decreases with increasing the salinity of spent ion-exchange resin regeneration solutions.
引用
收藏
页数:7
相关论文
共 50 条
  • [31] Use of ion-exchange membranes for the removal of tin from spent activating solutions
    Garcia-Gabaldon, M.
    Perez-Herranz, V.
    Garcia-Anton, J.
    Guinon, J. L.
    DESALINATION AND WATER TREATMENT, 2009, 3 (1-3) : 150 - 156
  • [32] MOLECULAR ADSORPTION AND ION-EXCHANGE OF WEAK ORGANIC ELECTROLYTES ON ION-EXCHANGE RESIN
    POCHHALI, L
    ADHIKARY, SK
    RAY, KC
    JOURNAL OF THE INDIAN CHEMICAL SOCIETY, 1977, 54 (09) : 889 - 893
  • [33] DESALINATION BY THERMALLY REGENERATED ION-EXCHANGE RESINS
    STEPHENS, GK
    BOLTO, BA
    EFFLUENT & WATER TREATMENT JOURNAL, 1977, 17 (03): : 116 - 122
  • [34] WATER DESALINATION BY ION-EXCHANGE HOLLOW FIBERS
    KORNGOLD, E
    VOFSI, D
    DESALINATION, 1991, 84 (1-3) : 123 - 135
  • [35] FRACTIONATION OF GELATIN BY ION-EXCHANGE RESIN
    TUOMINEN, T
    KULONEN, E
    ACTA CHEMICA SCANDINAVICA, 1959, 13 (10): : 2120 - 2120
  • [36] ION-EXCHANGE RESIN IN PREMENSTRUAL SYNDROME
    MUSTAKALLIO, M
    KINNUNEN, O
    LANCET, 1954, 1 (MAR20): : 627 - 627
  • [37] POLY(METHYL METHACRYLATE) AS INCORPORATION MEDIUM FOR SPENT ION-EXCHANGE RESIN - 2. SIMULATED RESIN.
    Ghattas, N.K.
    Ikladious, N.E.
    Eskander, S.B.
    Journal of Applied Polymer Science, 1983, 28 (05): : 1779 - 1786
  • [38] SEPARATION OF SUGARS ON AN ION-EXCHANGE RESIN
    SAUNDERS, RM
    CARBOHYDRATE RESEARCH, 1968, 7 (01) : 76 - &
  • [39] ION-EXCHANGE RESIN BEZOAR IN A NEONATE
    BERMAN, L
    BRIGGS, R
    THOMAS, RM
    CLINICAL RADIOLOGY, 1986, 37 (03) : 297 - 298
  • [40] ELECTROKINETIC BEHAVIOR OF ION-EXCHANGE RESIN
    FREEMAN, DH
    SCATCHARD, G
    SCIENCE, 1964, 144 (361) : 411 - &