| Raw-Water Intake and Screening | Removes large debris before chemical treatment and clarification. | Bar-screen openings commonly range from approximately 6 to 50 mm, depending on the intake design. | Leaves suspended particles and colloids in the water while retaining larger solids such as leaves and plastics. | Screen differential head, flow rate, debris loading, and intake water level. |
| Rapid Mixing | Disperses coagulant quickly and uniformly throughout the water. | Typical mixing time: about 10–60 seconds. Common velocity-gradient values are approximately 300–1,000 s−1. | Coagulant hydrolysis products neutralize particle charges and may form metal hydroxide precipitates that capture impurities. | pH, temperature, chemical dose, mixer speed, and mixing intensity. |
| Coagulant Addition | Destabilizes colloids that would otherwise remain suspended. | Common coagulant categories include aluminum salts, iron salts, and polymer-based aids. Dose must be established by jar testing; it is not a universal fixed value. | Reduces electrostatic repulsion and promotes particle collisions, aggregation, and adsorption. | Coagulant dose, alkalinity, pH, turbidity, dissolved organic carbon, and residual metal concentration. |
| Flocculation Basin | Gently brings destabilized particles together to form larger flocs. | Typical detention time: about 15–45 minutes. Common velocity-gradient values are approximately 20–80 s−1, often reduced through multiple stages. | Small microflocs collide and grow into stronger, settleable flocs without excessive shear. | Floc size, floc strength, basin short-circuiting, paddle speed, and visible carryover. |
| Flocculation Equipment | Provides controlled low-energy mixing using mechanical or hydraulic methods. | Common equipment includes horizontal or vertical paddles, turbine mixers, baffled channels, and hydraulic flocculators. | Maintains particle contact while limiting turbulence that could break formed flocs apart. | Motor speed, power draw, impeller condition, baffle condition, and floc-breakage signs. |
| Sedimentation Basin | Separates settleable flocs from clarified water by gravity. | Typical surface overflow rates for conventional clarification are approximately 20–60 m³/m²·day, subject to design and water quality. | Flocs settle to the basin floor, while clarified water flows toward collection launders or outlet structures. | Overflow rate, basin water level, turbidity, sludge blanket depth, and hydraulic short-circuiting. |
| Settling Time | Provides sufficient hydraulic residence time for flocs to separate. | Common detention times are approximately 2–4 hours in conventional sedimentation basins. | Gravity overcomes the upward or horizontal water movement for particles with adequate settling velocity. | Detention time, inlet and outlet flow distribution, temperature, and settled-water turbidity. |
| Tube or Plate Settlers | Increase effective settling area within a compact clarification footprint. | Inclined modules commonly use angles near 60° from horizontal, although the exact arrangement varies by design. | Shortens the vertical settling distance and encourages captured solids to slide down into the sludge zone. | Module fouling, hydraulic loading, channel distribution, and effluent turbidity. |
| Sludge Collection and Removal | Continuously or periodically removes concentrated solids from the basin. | Equipment may include scraper bridges, chain-and-flight collectors, suction headers, or hopper outlets. | Prevents excessive sludge accumulation, anaerobic conditions, and resuspension of settled flocs. | Sludge blanket depth, solids concentration, withdrawal frequency, torque, and odor formation. |
| Clarified-Water Outlet | Collects treated water evenly while minimizing disturbance to the settling zone. | Outlet launders and weirs are designed to distribute flow uniformly across the basin width. | Allows low-turbidity water to leave the sedimentation stage for filtration or other downstream treatment. | Effluent turbidity, weir loading, flow balance, floating solids, and visible floc carryover. |
| Typical Performance Indicators | Evaluates whether coagulation and sedimentation are functioning effectively. | Performance is site-specific; turbidity reduction, particle removal, and settled-water quality are normally verified through routine sampling. | Successful treatment converts stable colloids into larger flocs that can be removed by gravity. | Raw and settled-water turbidity, pH, alkalinity, temperature, coagulant dose, and jar-test results. |