Research Article
Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger
Table 1
Manufacturer data of the resin (Rohm and Haas 1998 [
20]).
| (a) The properties of the resin, Amberjet 1200Na |
| | Matrix | Styrene divinylbenzene copolymer | | Functional groups | Sulfonic acid | | Physical form | Insoluble, amber beads | | Ionic form as shipped | Sodium | | Total exchange capacity | 2.0 meq/mL minimum (Na+ form) | | Moisture holding capacity | 43 to 47% (Na+ form) | | Shipping weight | 53 lbs/ft3 | | Harmonic mean size | 0.57 to 0.67 mm | | Uniformity coefficient | 1.2 maximum | Maximum reversible swelling | Approximately 10% (from Na+4 form to hydrogen) |
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| (b) Suggested operating conditions of the resin |
| | pH range | 0 to 14 | | Maximum operating temperature | 250°F | | Minimum bed depth | 24 inch minimum | | Service flow rate | 1 to 6 gpm/ft3 | | Maximum service velocity | 25 gpm/ft2 | | Regenerants (100%) | NaCl | HCl | H2SO4 | | Flow rate (gpm/ft3) | 2 to 8 | 2 to 5 | 2 to 20 | | Concentration (%) | 10 | 4 to 10 | 1 to 8 | | Level (lbs/ft3) | 3 to 15 | 2 to 8 | 2.5 to 12.5 | | Minimum contact time | 20 minutes | | Slow rinse | 15 gal/ft3 at regeneration flow rate | | Fast rinse | 8 to 22 gal/ft3 at service flow rate |
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