After addition to water, aluminum sulfate and ferric chloride hydrolyze, producing positively charged hydrolysis products and metal hydroxide precipitates. These products interact with suspended and colloidal particles in different but complementary ways: charged species reduce particle repulsion, while precipitates provide surfaces that can capture contaminants. The resulting chemical changes enable particles to gather into separable flocs.
Performance depends on controlling dosage, pH, and mixing conditions because these variables influence hydrolysis, particle destabilization, and contact between coagulant products and contaminants. An unsuitable dosage or pH can reduce treatment effectiveness, while inadequate mixing can limit interactions throughout the liquid. Optimizing these conditions helps improve removal while limiting residual metals and unnecessary sludge production.
Charge neutralization occurs when positively charged hydrolysis products reduce the electrical repulsion that keeps colloidal particles dispersed. Adsorption allows contaminants or particles to attach to available surfaces, while sweep flocculation occurs as forming metal hydroxide precipitates capture particles within the developing floc. Together, these mechanisms convert difficult-to-separate material into aggregates that can be removed by sedimentation.
A practical sequence begins by adding the selected metal salt to the liquid, followed by mixing that promotes contact between hydrolysis products and suspended or colloidal particles. As destabilized material and metal hydroxide precipitates form flocs, the treatment proceeds to sedimentation, where the aggregates separate from the clarified liquid. Dosage, pH, and mixing conditions require adjustment for effective performance.
These coagulants are relevant to both drinking-water and wastewater treatment. Their use can reduce turbidity and suspended solids, and it can often lower phosphate concentrations as well. The appropriate operating conditions depend on the treatment objective and water chemistry, so controlling dosage and pH is important when applying the process to different liquid-treatment settings.
Evaluation should include reductions in turbidity, suspended solids, and, where relevant, phosphate, alongside possible residual metal concentrations and sludge production. Strong removal performance does not eliminate the need to assess these secondary outcomes. Comparing dosage and operating conditions helps identify a treatment balance that achieves the desired contaminant reduction without creating excessive residual metals or sludge.