Czasopismo
Tytuł artykułu
Warianty tytułu
Języki publikacji
Abstrakty
Performance of cation and anion exchangers was evaluated by carrying out breakthrough analyses of pH, conductivity, free mineral acid (FMA) and various dissolved solids for an industrial water treatment plant of 700 gpm capacity. The breakthrough curves showed no leakage of calcium, magnesium and chloride throughout the operating period of the train, however, they indicated the early leakage of sodium, potassium, sulphate and silica. The operating/breakthrough capacity, total capacity and degree of column utilization were determined. The column utilization was found to be 67.85%, 38.93% and 16.78% against the design values of 90%, 85% and 85% for cation, primary and secondary anion exchangers respectively. The operating time of the water treatment train was significantly increased by achieving adequate capacity utilization of secondary anion exchanger. The low capacity utilization of secondary anion resin due to early silica slippage, has been discussed in the paper.
Czasopismo
Rocznik
Tom
Numer
Strony
35-41
Opis fizyczny
Daty
wydano
2012-01-01
online
2012-07-02
Twórcy
autor
- Department of Chemical Engineering, University of Engineering and Technology Lahore, Pakistan
autor
- Department of Chemical Engineering, University of Engineering and Technology Lahore, Pakistan
autor
- Department of Chemical Engineering, University of Engineering and Technology Lahore, Pakistan
autor
- Dawood Hercules Chemicals Limited, Lahore, Pakistan
autor
- Dawood Hercules Chemicals Limited, Lahore, Pakistan
Bibliografia
- Noh, B. I., Lee, C. W., Yoon, T. K., Moon, B. H., Lee, G. C. & Shin, C. H. (1999). Parametric Studies on the Performance of Mixed-Bed Ion Exchange at Ultralow Concentration. Korean J. Chem. Eng. 16(6), 737-744. DOI: 10.1007/BF02698345.[Crossref]
- Kunin, R. & McGarvey, E. X. (1964). Ion Exchange, Ind. Eng. Chem. 56 (10), 53-56, DOI: 10.1021/ie50658a009.[Crossref]
- Kunin, R. & Gustafson, R. L. (1967). Ion Exchange, Ind. Eng. Chem. 59(11), 95-100, DOI: 10.1021/ie50695a013.[Crossref]
- Clifford, D. A. (1996). Ion Exchange and Inorganic Adsorption. In Letterman R. D. (5th Eds.). Water Quality and Treatment - A Handbook of Community Water Supplies (pp 9.1-9.91). McGraw Hill.
- Chowdiah, V. & Foutch, G. L., (1995). A Kinetic Model for Cationic-Exchange-Resin Regeneration. Ind. Eng. Chem. 34(11), 4040-4048. DOI: 10.1021/ie00038a045.[Crossref]
- Beyer, W. A. & James, D. B. (1966). Independence of Performance of Ion-Exchange Column on Its Shape, Ind. Eng. Chem. 5(3), 433-434. DOI: 10.1021/i160019a024.[Crossref]
- Clifford, D. (1982). Multicomponent ion-exchange calculations for selected ion separations, Ind. Eng. Chem. Fundamen. 21(2), 141-153. DOI: 10.1021/il00006a008.[Crossref]
- Ahmed, R.A, Ahmad, A., Omar, M. & Kadir, A. (2008). Studies on Breakthrough Lime of Strong Cation Exchange Resin in a Water Treatment Plant, 28-30 May 2008 (pp 880-885), penang, Malaysia, ICERT,.
- Vermeulen, T. & Huffman, E. H. (1953). Ion Exchange Column Performance Hydrogen Cycle Rates in Nonaqueous Solvents, Ind. Eng. Chem. 45(8), 1658-1664. DOI: 10.1021/ie50524a024.[Crossref]
- Frisch, N. & Kunin, R. (1957). Long-Term Operating Characteristics of Anion Exchange Resins, Ind. Eng. Chem. 49(9), 1365-1372. DOI: 10.1021/ie50573a028.[Crossref]
- Helfferich, F. (1962). Ion Exchnage, Mc Graw Hill, New Ýork, 424.
- Mindick, M. (1955). Capacity and Leakage of Ion Exchange Columns, Ind. Eng. Chem. 47(1), 96-101 DOI: 10.1021/ie50541a035.[Crossref]
- Ning, R. Y. (2002). Discussion of silica speciation, fouling, control and maximum reduction, Desalination. 151, 67-73 Doi.10.1016/S0011916402009736.[Crossref]
- Ali, M. B. S., Hamrounl, B., Bouguecha, S. & Dhahbi, M. (2004). Silica removal using ion-exchange resins, Desalination. 167, 273-279, doi/10.1016/j.desal.2004.06.136.[Crossref]
Typ dokumentu
Bibliografia
Identyfikatory
Identyfikator YADDA
bwmeta1.element.-psjd-doi-10_2478_v10026-012-0068-3