South Carolina’s Municipal Sewage Treatment Plants: 2025 Data & Trends
South Carolina operates 161 publicly owned wastewater treatment plants (POTWs) serving 3.75 million residents, with capacities ranging from 0.1 MGD to 36 MGD. The largest, Columbia Metro WWTP, treats 35 MGD using conventional activated sludge, while Charleston’s Plum Island facility achieves 36 MGD with primary and secondary treatment. All plants must comply with EPA’s NPDES permits and SC DHEC’s Water Quality Standards, which mandate effluent limits of 30 mg/L BOD₅, 30 mg/L TSS, and 10 mg/L ammonia-N. Emerging contaminants like PFAS are not yet federally regulated but are under SC DHEC monitoring, with potential future limits below 70 ppt (SC DHEC 2024 draft).
The state’s wastewater infrastructure is currently undergoing a significant transition as the 10 largest plants handle approximately 45% of the total municipal flow. Population served per plant varies drastically, from rural systems serving fewer than 1,000 residents to the Columbia Metro WWTP serving over 314,000 people. According to the SC DHEC 2025 Resilience Plan, 40% of coastal facilities, including Charleston Water System’s Plum Island, are now prioritizing flood-proofing and climate vulnerability assessments to mitigate sea-level rise and storm surge risks. Regulatory pressure is also mounting regarding nutrient removal, particularly for facilities discharging into sensitive watersheds like the Savannah River or Lake Marion.
| Rank | Facility Name | Operator | City | Population Served (2022) |
|---|---|---|---|---|
| 1 | Metro WWTP | City of Columbia | Columbia | 314,797 |
| 2 | Mauldin Rd Plant | ReWa | Greenville | 243,177 |
| 3 | Plum Island WWTP | Charleston Water System | Charleston | 232,756 |
| 4 | Horse Creek TF | Aiken County | Beech Island | 118,400 |
| 5 | Grand Strand WWTP | GSWSA | Myrtle Beach | 95,000 |
Engineering Specs for South Carolina POTWs: Process Flows, Effluent Quality & Compliance Benchmarks
Conventional activated sludge (CAS) remains the dominant secondary treatment process in South Carolina, utilized by 68% of the state's POTWs, though Membrane Bioreactor (MBR) adoption has risen to 12% in high-growth urban corridors. A typical 10 MGD CAS plant in the state involves a process flow consisting of mechanical bar screening, grit removal, primary clarification, aeration basins with fine-bubble diffusers, and secondary clarification. For plants requiring higher effluent standards, MBR systems for South Carolina POTWs provide a streamlined alternative by combining aeration and solids separation into a single stage, achieving significantly lower turbidity and nutrient levels.
Effluent quality benchmarks are strictly governed by NPDES permits, with standard requirements of BOD₅ ≤30 mg/L and TSS ≤30 mg/L. Seasonal ammonia-N limits are increasingly common, often set at 10 mg/L during summer months and 20 mg/L during winter to protect dissolved oxygen levels in receiving streams. Disinfection trends are shifting away from chlorine gas (currently 45% of plants) toward UV radiation (30%) and chlorine dioxide (15%) to avoid the formation of disinfection byproducts (DBPs) and simplify safety compliance under SC DHEC 2023 guidelines. Sludge handling varies by scale; while 55% of plants utilize aerobic digestion, larger facilities are increasingly adopting anaerobic digestion for biogas recovery or lime stabilization for land application in rural agricultural zones.
| Parameter | Conventional Activated Sludge (CAS) | Membrane Bioreactor (MBR) | SC DHEC/EPA Benchmark |
|---|---|---|---|
| Hydraulic Retention Time (HRT) | 18–24 Hours | 6–10 Hours | N/A |
| Solids Retention Time (SRT) | 10–20 Days | 25–50 Days | N/A |
| Effluent BOD₅ | 15–30 mg/L | <5 mg/L | 30 mg/L |
| Effluent TSS | 15–30 mg/L | <1 mg/L | 30 mg/L |
| Effluent Ammonia-N | 5–10 mg/L | <1 mg/L | 10 mg/L (Summer) |
Technology Comparison: Conventional vs. MBR vs. Advanced Treatment for SC POTWs

Membrane Bioreactor (MBR) technology requires a 60% smaller physical footprint than conventional activated sludge systems, making it the preferred choice for urban expansions where land acquisition costs are prohibitive. While CAS systems offer the lowest initial CAPEX—ranging from $5M to $15M for facilities between 5 and 30 MGD—they require extensive secondary clarification and tertiary filtration to match the effluent quality naturally produced by membranes. For municipalities discharging into nutrient-sensitive watersheds, such as those feeding the Waccamaw River, advanced treatment incorporating tertiary filtration and DAF systems for FOG and TSS removal is often necessary to meet phosphorus limits as low as 0.1 mg/L.
The trade-off for higher effluent quality and smaller footprints is found in operational intensity and energy consumption. CAS systems typically operate at 0.5–0.8 kWh/m³, whereas MBR systems range from 0.8–1.2 kWh/m³ due to the air scouring required to prevent membrane fouling. Advanced tertiary systems can reach 1.5 kWh/m³ when high-intensity UV and ozone stages are included. Decision-makers must weigh these lifecycle costs against the benefits of deferred land purchases and the potential for water reuse, which is becoming a viable strategy for drought-prone regions of the South Carolina Upstate.
| Feature | Conventional (CAS) | MBR System | Advanced (Tertiary) |
|---|---|---|---|
| Footprint (10 MGD) | 2.5–4.0 Acres | 0.8–1.2 Acres | 3.0–5.0 Acres |
| Effluent Quality | Standard Compliance | Superior/Reuse Quality | Nutrient Removal Focus |
| Energy Use (kWh/m³) | 0.5–0.8 | 0.8–1.2 | 1.0–1.5 |
| CAPEX (10 MGD) | $10M – $12M | $18M – $22M | $25M – $30M |
| OPEX ($/1,000 gal) | $0.80 – $1.20 | $1.50 – $2.50 | $2.00 – $3.50 |
Cost Breakdown: CAPEX, OPEX & ROI for South Carolina Sewage Treatment Plants
Capital expenditures for new South Carolina POTWs in 2025 range from $1.0 million to $1.2 million per MGD for conventional plants, while MBR-based facilities average $1.8 million to $2.2 million per MGD. These figures encompass civil engineering, mechanical equipment, electrical integration, and SC DHEC permitting fees. While the initial investment for MBR is higher, lifecycle cost analyses from the EPA (2024) indicate that MBR systems can achieve 20% lower total costs over a 20-year horizon when accounting for reduced sludge disposal volumes and the elimination of secondary clarifier maintenance. For a broader perspective on regional financial requirements, engineers can compare these figures against global cost benchmarks for POTWs to validate local procurement bids.
Operational expenditures (OPEX) are driven primarily by energy, labor, and chemical dosing requirements. Implementing automatic chemical dosing systems can reduce coagulant and polymer waste by up to 30%, significantly impacting the bottom line for plants exceeding 5 MGD. A notable regional case study is Charleston’s Daniel Island MBR plant, which successfully reduced its annual OPEX by 25% by eliminating the need for secondary clarification and reducing the volume of sludge hauled to landfills. ROI for such upgrades is typically realized within 5 to 8 years through energy-efficient blower upgrades (using VFDs) and automated process controls that minimize manual labor hours.
| Cost Component (10 MGD) | Conventional (CAS) | MBR System | ROI Driver |
|---|---|---|---|
| Mechanical Equipment | $4.5M | $9.0M | Membrane Longevity |
| Civil & Construction | $5.5M | $3.0M | Reduced Land Use |
| Annual Energy Cost | $420,000 | $680,000 | VFD Efficiency |
| Annual Sludge Disposal | $180,000 | $110,000 | Higher Solids Content |
| Estimated 20-Yr NPV | $24.5M | $21.8M | Lower Lifecycle OPEX |
Equipment Selection Guide: Zero-Risk Choices for SC POTWs

Primary treatment efficiency in South Carolina plants is maximized by utilizing rotary mechanical bar screens with 6mm spacing, which are capable of removing 95% of large solids and inorganic debris before they reach sensitive downstream pumps. For secondary treatment, the choice between MBR and CAS should be dictated by effluent requirements; urban plants facing strict nutrient limits benefit most from high-flux membrane modules, while rural plants with ample land often find CAS more economical. To ensure compliance with Alabama’s neighborly standards or similar regional requirements, engineers may also reference