| Coagulation | Destabilizes suspended and colloidal particles so they can combine into larger particles. | Turbidity Clay Colloids Natural organic matter | Hydrolyzed aluminum species reduce particle charge and form aluminum hydroxide flocs that capture impurities. | Rapid mixing, immediately after chemical dosing. | Dose selection depends on raw-water turbidity, alkalinity, temperature, pH, organic content, and the PAC formulation. |
| Flocculation | Supports the growth of small destabilized particles into settleable or filterable flocs. | Fine suspended solids Colloidal matter | Gentle mixing allows microflocs to collide and form larger aggregates without breaking them apart. | Slow-mix basin after coagulation. | Mixing intensity and detention time must be controlled; excessive turbulence can shear the flocs. |
| Sedimentation and Clarification | Improves the removal of chemically formed flocs before filtration. | Settled solids Turbidity Color | Dense aluminum-based flocs settle by gravity and carry adsorbed or entrapped impurities out of the water. | Clarifiers, settling tanks, or lamella settlers. | Hydraulic loading, sludge withdrawal, and floc strength affect clarification performance. |
| Direct Filtration | Reduces the particle load entering filters and improves filter-water quality. | Low-to-moderate turbidity Residual colloids Fine particles | PAC creates flocs that are retained within granular media or other filtration media. | After rapid mixing and flocculation, without a full sedimentation step. | Suitable only when raw-water solids loading is compatible with the filter design; excessive dosing may shorten filter runs. |
| Conventional Drinking-Water Treatment | Provides chemical clarification as part of a multi-barrier treatment train. | Turbidity Apparent color Organic matter Microorganism-associated particles | Coagulation and floc removal lower the particle burden before filtration and disinfection. | Typically before clarification, filtration, and final disinfection. | PAC does not replace disinfection; finished water must meet applicable drinking-water requirements. |
| Color Removal | Reduces visible color caused by dissolved or colloidally dispersed substances. | Humic substances Fulvic substances Industrial color bodies | Aluminum hydrolysis products adsorb and enmesh some color-causing compounds in the formed floc. | Coagulation followed by clarification or filtration. | Color removal varies with pH, molecular characteristics, alkalinity, and the source of the colored water. |
| Phosphorus Removal | Converts soluble phosphate into insoluble aluminum phosphate or incorporates it into aluminum-rich flocs. | Orthophosphate Total phosphorus | Aluminum reacts with phosphate and the resulting solids are removed by settling or filtration. | Biological nutrient-removal polishing, tertiary treatment, or chemical precipitation. | Stoichiometric demand, competing reactions, pH, and sludge production must be considered. |
| Industrial Wastewater Clarification | Separates suspended and emulsified material from process wastewater. | Suspended solids Emulsified oils Metals associated with solids Color | Charge neutralization and sweep flocculation produce solids that can be separated in a clarifier or dissolved-air flotation unit. | After equalization and pH adjustment; before biological or polishing treatment. | Jar testing is important because wastewater composition can change significantly during production cycles. |
| Dissolved Air Flotation | Creates flocs that attach to fine air bubbles and rise to the surface. | Low-density solids Algae Fats, oils, and grease | PAC destabilizes particles, while recycled pressurized water supplies bubbles that float the floc. | Coagulation and flocculation immediately before flotation. | Floc size, bubble distribution, recycle ratio, and surface loading influence performance. |
| Sludge Conditioning | Can improve dewaterability and solids capture in selected sludge streams. | Water-treatment sludge Fine solids | Aluminum-based coagulation can promote aggregation of fine particles before thickening or dewatering. | Before gravity thickening, flotation thickening, filtration, or centrifugation. | Effectiveness is sludge-specific; chemical addition may increase ash content and residual aluminum in the cake. |
| Pretreatment for Membrane Systems | Reduces particulate and colloidal loading that can contribute to membrane fouling. | Turbidity Colloids Natural organic matter | Coagulation followed by clarification or filtration removes foulant precursors before membrane separation. | Upstream of microfiltration, ultrafiltration, nanofiltration, or reverse osmosis. | Residual aluminum and carryover flocs must be controlled to protect membranes and maintain stable operation. |