| Low to moderate turbidity in surface water | Fine suspended clay, silt, and mineral particles; turbidity commonly below 500 NTU | Low to medium charge density; medium to high molecular weight; supplied as a water-soluble powder or emulsion | Particle bridging and faster clarification | Use after inorganic coagulant addition when required. Avoid excessive mixing after flocs form. |
| High turbidity or heavy mineral solids | Large quantities of clay, sand, or suspended mineral solids; rapidly settling or dense solids | Medium to high molecular weight; medium charge density; strong floc-forming performance | Increase floc size, settling rate, and solids capture | Confirm that the product does not produce overly large, weak, or shear-sensitive flocs. |
| Mineral processing and tailings water | Fine mineral particles, high suspended solids, variable ionic strength, and possible metal ions | High molecular weight; charge density selected according to mineral surface chemistry and water conductivity | Solid-liquid separation and improved thickener or clarifier performance | Run jar tests using actual process water because salinity and dissolved ions can strongly affect flocculation. |
| Wastewater containing suspended organic solids | Activated sludge, biological solids, food-processing residues, or other negatively charged particles | Medium charge density with medium to high molecular weight; compatibility with biological sludge should be verified | Improve sludge settling, thickening, and dewatering | Evaluate capillary suction time, specific resistance to filtration, filter-cake moisture, and filtrate clarity. |
| Sludge dewatering by belt press or centrifuge | High water content, compressible sludge, poor drainage, or cloudy filtrate | Often medium to high molecular weight; charge density and solution viscosity selected by equipment type | Release bound water and produce a stronger, drier sludge cake | The optimum dose depends on sludge age, solids concentration, shear, polymer aging, and feed-point location. |
| Neutral to alkaline process water | pH approximately 6.5–9.0 with stable water chemistry | Standard anionic PAM grades may be suitable; select hydrolysis level according to particle charge and ionic strength | Flocculation, clarification, or sludge conditioning | Check performance across the actual operating pH range rather than relying only on laboratory water. |
| High salinity or elevated conductivity | High dissolved-solids concentration, brackish water, or substantial calcium and magnesium levels | A grade with demonstrated salt tolerance; molecular weight and charge density must be verified by testing | Maintain floc formation under elevated ionic strength | High salt levels can reduce polymer expansion and change settling behavior. Test with representative water samples. |
| Low-temperature water | Water temperature commonly below 10 °C; slower particle collision and settling | A grade that hydrates reliably at low temperature; molecular weight should be balanced against solution-mixing requirements | Compensate for slower flocculation and settling kinetics | Allow sufficient maturation time after preparation and verify floc strength at actual temperature. |
| Very fine or colloidal particles | Low settling velocity, persistent cloudiness, and particles that remain suspended after conventional mixing | Higher charge density or higher molecular weight may be required, depending on particle surface charge and pretreatment | Destabilize colloids and create settleable or filterable flocs | Anionic PAM is often used as a flocculant after charge neutralization; it may not replace the primary coagulant. |
| Polishing filtration after clarification | Residual turbidity or fine floc entering sand, multimedia, or membrane pretreatment | Low-dose, high-efficiency grade selected to minimize residual polymer and filter loading | Improve filtrate clarity and protect downstream equipment | Monitor residual turbidity, differential pressure, filter run time, and possible membrane fouling. |