Anion exchange resins are characterized by two main capacities:
- Total (Theoretical) Capacity – maximum number of exchange sites
- Operating (Working/Breakthrough) Capacity – usable capacity in real conditions
1. Total Exchange Capacity of Anion Exchange Resin
Standard Method for Strong Base Anion (SBA) Resins (Type I & Type II)
Principle
Convert resin to Cl⁻ form → displace Cl⁻ with excess Na₂SO₄ or NaNO₃ → titrate liberated Cl⁻ with AgNO₃.
Reagents
- 1 M NaOH
- 1 M HCl
- 5–10% Na₂SO₄ or NaNO₃ solution
- 0.1 M AgNO₃
- Potassium chromate indicator (K₂CrO₄)
Procedure
- Weigh accurately 1.0 g of wet resin (or 0.5 g dry) in OH⁻ form.
- Convert completely to Cl⁻ form:
- Pass 200–300 mL of 5% NaCl or 1 M HCl slowly through a small column.
- Wash with distilled water until effluent is chloride-free and neutral.
- Regenerate to displace chloride:
- Pass 200 mL of 10% Na₂SO₄ (or 1 M NaNO₃) very slowly (2–4 mL/min).
- Collect effluent + washings in a 500 mL volumetric flask.
- Wash with distilled water until total volume ≈ 500 mL.
- Dilute to exactly 500 mL.
- Take 50.0 mL aliquot and titrate with 0.1 M AgNO₃ using 5% K₂CrO₄ indicator (Mohr method) until brick-red end point.
Calculation
Total Capacity (meq/g) = (V × N × 10) / W
Where:
V = mL of AgNO₃ used
N = normality of AgNO₃
10 = dilution factor (500/50)
W = weight of resin (g)
For Weak Base Anion (WBA) Resins
Use acid titration:
- Convert resin to free base (FB) form with 1 M NaOH and wash.
- Pass excess 1 M HCl → collect effluent.
- Titrate excess HCl with 0.1 M NaOH to find how much acid was consumed by the resin.
Capacity (meq/g) = (Initial HCl − Excess HCl) / weight of resin
2. Operating (Breakthrough) Capacity
Measured exactly like cation resins but with anions (e.g., chloride, sulfate, silica, or real water).
Typical Procedure
- Pack 100 mL of resin (in Cl⁻ or OH⁻ form) in a column.
- Pass feed water with known anion concentration (e.g., 500 mg/L as CaCO₃ alkalinity + chloride) at constant flow rate.
- Monitor effluent for the target anion until breakthrough (usually when effluent reaches 1–5% of influent).
- Continue until complete exhaustion.
Calculation
Operating Capacity (eq/L) = (C₀ × Vₑ) / Vᵣ
C₀ = influent anion concentration (eq/L)
Vₑ = volume treated until chosen endpoint (L)
Vᵣ = resin volume (L)
Summary of Typical Values
| Resin Type | Total Capacity (eq/L wet) | Typical Operating Capacity (eq/L) |
|---|---|---|
| Strong Base Type I (gel) | 1.2 – 1.4 | 0.6 – 1.0 |
| Strong Base Type II (gel) | 1.3 – 1.5 | 0.8 – 1.1 |
| Strong Base Macroporous | 0.9 – 1.2 | 0.6 – 0.9 |
| Weak Base (gel/macroporous) | 1.5 – 2.2 | 1.0 – 1.8 |
Related Topics:
Determination of Cation Exchange Resin Capacity
Mixed Bed Ion Exchange Resin Capacity
Mixed-Bed Deionization