| Conventional activated sludge | Air is supplied to a biological reactor where microorganisms consume organic pollutants; a secondary clarifier separates the settled biomass from treated water. | Well-established process; can achieve substantial removal of biodegradable organic matter and suspended solids. | Requires aeration energy, process monitoring, and management of excess sludge; performance depends on stable operating conditions. | Medium and large communities where reliable secondary treatment is required. |
| Sequencing batch reactor (SBR) | A tank treats wastewater in timed cycles that typically include filling, biological reaction, settling, and decanting. | Combines biological treatment and settling in the same basin; cycle conditions can be adjusted to support nitrogen removal. | Needs automated controls and careful cycle management; flow peaks must be accommodated in the operating schedule or tank capacity. | Small to medium-sized communities and sites with limited room for separate process tanks. |
| Oxidation ditch | Wastewater circulates through an oval or looped channel, where aeration and biological treatment take place before solids are settled. | Can provide stable treatment and, with suitable design and operation, biological nitrogen removal. | The channel layout can require a relatively large site; aeration and circulation equipment need ongoing operation and maintenance. | Small and medium communities seeking a robust activated-sludge process. |
| Trickling filter | Wastewater is distributed over a bed of media covered by a microbial film; air moving through the bed supports biological treatment. | Generally has lower aeration requirements than fully aerated suspended-growth processes and can be operationally straightforward. | May need recirculation and downstream clarification; media distribution and ventilation affect performance. | Communities seeking a fixed-film biological process, including facilities upgrading or expanding existing treatment. |
| Rotating biological contactor (RBC) | Partially submerged rotating discs provide surfaces for microbial growth and alternate the biofilm between wastewater and air. | Provides attached-growth treatment in a compact arrangement and can be suitable for smaller flows. | Mechanical components require maintenance; a clarifier is commonly used to remove sloughed biological solids. | Small communities and decentralized municipal facilities. |
| Membrane bioreactor (MBR) | Biological treatment is combined with membrane filtration to separate treated water from suspended solids, often replacing secondary clarifiers. | Produces low-solids effluent and can support a smaller treatment footprint; treated water may be suitable for further polishing and reuse, subject to requirements. | Membranes need cleaning and eventual replacement; energy use and operating costs can be higher than for some conventional systems. | Space-constrained facilities and projects with stringent effluent or reuse goals. |
| Waste stabilization ponds (lagoons) | Wastewater is retained in shallow or deep ponds, where settling and natural biological processes reduce pollutants over time. | Can use relatively simple equipment and low mechanical energy input; operations are generally less complex than intensive mechanical processes. | Requires substantial land and adequate retention time; performance can be affected by temperature, weather, and seasonal conditions. | Smaller or less densely populated communities with available land and suitable local conditions. |