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AMD Chemistry and Neutralisation Fundamentals

AMD Generation: FeS₂ + ¾ O₂ + H₂O → Fe²⁺ + 2 SO₄²⁻ + 2 H⁺. Ferrous iron then oxidises: Fe²⁺ + ¼ O₂ + H⁺ → Fe³⁺ + ½ H₂O. At pH > 3.5, Fe³⁺ hydrolyses: Fe³⁺ + 3 H₂O → Fe(OH)₃↓ + 3 H⁺. Aeration accelerates Fe(II) oxidation 10³–1⁰⁴× relative to quiescent conditions, reducing the acid load entering solution.

Neutralisation Reagent Comparison

ReagentTarget pH RangeNeutralisation Eq. (kg/kg H₂SO₄)Sludge ProductionTypical Application
Hydrated lime Ca(OH)₂8.0–9.50.76High (CaSO₄ + Fe(OH)₃)High-acidity AMD, rapid pH lift
Limestone (CaCO₃)6.0–7.51.02ModeratePassive limestone beds, low-acidity systems
Soda ash (Na₂CO₃)7.0–9.01.06LowHigh-salinity AMD; avoids Ca scaling
Caustic soda (NaOH)Any target0.82LowTrim dosing after lime stage; pH fine control
Anoxic limestone drain (ALD)5.5–7.0PassiveVery lowLow-Fe, low-Al AMD pre-treatment

Aeration Role in Acidity Treatment

Aeration serves two functions in AMD treatment: (1) oxidising Fe(II) to Fe(III), shifting the hydrolysis equilibrium and generating alkalinity-consuming precipitate before discharge; (2) CO₂ stripping from carbonate-buffered systems after lime addition to raise pH past 8.3 where carbonate rather than bicarbonate dominates. A correctly sized diffused-air cascade before the lime contact tank can reduce lime consumption by 15–30% by oxidising iron before the neutralisation stage.

6-Step AMD Treatment Programme

1

Characterise Acidity Load

Full AMD chemistry profile: titratable acidity (mg/L CaCO₃ equivalent), free acidity, metal speciation (dissolved vs. colloidal Fe, Al, Mn). Calculate 90th percentile influent load (kg H₂SO₄/day) to size reagent systems.

2

Select Neutralisation Strategy

Choose active (lime/NaOH dosing) vs. passive (ALD, successive alkalinity-producing reactors — SAPR) based on flow rate, acidity load and discharge target. High-volume, high-acidity pit lakes almost always require active treatment.

3

Design Oxidation Aeration

Install diffused-air aeration upstream of neutralisation contact: airflow 3–8 m³ air/m³ water at 2–4 m water depth. Cascade aerators or sparge tubes both work; diffused air provides highest O₂ utilisation at depth.

4

Size Lime Contact Tank

Retention time 20–40 min at design flow. pH probe and feedback dosing with proportional-integral control; maintain pH 8.3–9.0 for complete Fe(III) precipitation and partial Mn removal.

5

Sludge Handling Design

AMD sludge is poorly settling (1–3% TS); thickening to 8–15% requires lamella clarifiers or centrifuges. Plan for 0.5–3 t sludge (dry) per t of AMD acidity neutralised. Consider filter-press dewatering for landfill disposal.

6

Monitoring and Consent Compliance

Continuous pH, conductivity, flow and DO monitoring at discharge. Weekly metals analysis (ICP-MS) against EA consent limits. Quarterly alkalinity titrations to confirm buffering capacity. Annual review of lime consumption vs. acidity load trends.

Equipment Options

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