Subsequent Treatment Solution: Polishing And Nutrient Removal
A subsequent treatment solution is the polishing stage that follows primary settling and the main biological (often anaerobic) step. It removes nitrogen, phosphorus, and residual organics - typically through an anoxic-aerobic (A2/O) or sequencing train - so the effluent meets a tight discharge limit. The tankage is usually bolted Glass-Fused-to-Steel reactors and clarifiers chosen for corrosion resistance and fast assembly.

Why Subsequent Treatment Exists
Primary treatment only drops settleable solids, and the main anaerobic or secondary stage removes most carbon but not nutrients. Many permits now cap total nitrogen and total phosphorus, which the earlier stages leave in solution. Subsequent treatment is the stage that strips those out before discharge.
| Stage | Removes | Typical Equipment |
| Primary | Settleable solids | Clarifier |
| Main biological | COD, BOD, some N | Anaerobic or activated sludge |
| Subsequent (polishing) | Remaining N, P, residuals | A2/O or SBR, filter |
How Nutrients Are Removed
An anoxic-aerobic sequence removes nitrogen: nitrate is formed in the aerobic zone and returned to the anoxic zone where it is denitrified to nitrogen gas. Phosphorus is captured by controlled sludge age or chemical addition. The train is sized only after the upstream load is defined, not as a generic add-on.
A Boundary Condition
Subsequent treatment cannot fix an undersized upstream stage; if the anaerobic or secondary train is overloaded, polishing will simply inherit the deficit. The polishing volume must be sized to the actual residual load, and the return flows must be balanced so the anoxic zone has carbon to denitrify.
Project Case Study: Domestic Sewage Treatment Project In Ghana
Project / Application: Municipal domestic sewage treatment, Ghana. Industry: Municipal. Tank Type: Glass-Fused-to-Steel (GFS). Key Requirements: Reliable nitrogen and phosphorus removal at community scale.
| Field | Value | Source / Evidence |
| Daily Treatment Volume | 1,800 m3/day | Company project reference |
| Reactor Types | UBF + A2/O + Sedimentation | Company project reference |
| UBF Tank | 1 set, O11.46 x 9.6 m | Company project reference |
| Secondary Sedimentation | 1 set, O14.52 x 4.8 m | Company project reference |
| A2/O Tanks | 2 sets, Outer O20.64 x 6.6 m | Company project reference |
| Installation Year | 2021 | Company project reference |
| Parameter | Influent | Effluent |
| COD Cr | 1,000 mg/L | 100 mg/L |
| BOD5 | 500 mg/L | 25 mg/L |
| Ammonia N | 30 mg/L | 10 mg/L |
| SS | 400 mg/L | 25 mg/L |
| Total P | 10 mg/L | 2 mg/L |
| pH | not stated | 6.5 to 9.0 |
About The Supplier
Shijiazhuang Zhengzhong Technology Co., Ltd (Center Enamel) manufactures Glass-Fused-to-Steel tanks rated for municipal and industrial polishing duty, with enamel firing at 820-930 C and certifications including ISO 9001, NSF/ANSI 61, and CE-EN 1090. The bolted system supports rapid overseas deployment and factory-controlled quality.
Comparison: Polishing Technologies
| Technology | Best For | Note |
| A2/O | Nitrogen and phosphorus | Compact, integrated |
| SBR | Variable loads | Flexible cycle |
| Sand or membrane filter | Tight final polish | Higher capital |
A subsequent treatment solution is where permits are actually met or missed. Design it from the residual load the upstream stage hands it, and choose tankage that lets the whole train be built and commissioned on schedule.
Frequently Asked Questions
Q1: What is subsequent treatment? A1: The polishing stage after primary and the main biological step, removing nitrogen, phosphorus, and residuals.
Q2: Why polish after anaerobic stages? A2: Anaerobic and secondary stages remove carbon but not nutrients, which tight permits now cap.
Q3: How are nutrients removed? A3: An anoxic-aerobic sequence strips nitrogen; controlled sludge age or chemicals capture phosphorus.
Q4: Which tankage suits polishing? A4: GFS reactors and clarifiers resist corrosion and assemble faster than concrete.
Q5: What is an A2/O? A5: An anaerobic-anoxic-aerobic train that removes carbon, nitrogen, and phosphorus in one circuit.
Q6: Can polishing be skipped? A6: Only when the permit allows; most modern permits require nutrient limits.
Q7: How fast can tankage be built? A7: One overseas municipal plant installed several GFS tanks for a 1,800 m3/day train.
Q8: Do all plants need subsequent treatment? A8: Only those with nutrient or tight reuse limits; many plants stop after secondary.
Describe your upstream load and discharge permit to an engineer, or request a subsequent treatment and tankage plan.