Design Manual › Secondary › Rectangular
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Rectangular Secondary Clarifier
The rectangular tank trades the circular scraper for a chain-and-flight mechanism and buys
a much better footprint on tight sites. It brings a check the circular design does not: horizontal
velocity. Push the water through too fast and you scour the blanket off the floor and carry it over
the weir.
1Duty & sludge
Secondary clarification is governed by two different limits at once — how fast water
rises (SOR) and how much solids the tank can pass to the bottom (SLR). Set both.
2Sizing criteria & geometry
Area takes the envelope of the hydraulic and solids limits. Length-to-width then sets the
plan: long and narrow gives better hydraulic efficiency, but a very long tank needs more scraper power.
Results — area envelope & geometry
Total area
—m²
HRT at avg flow
—h
Horizontal v
—m/min
| Item | Value | Basis |
|---|
3Hydraulics & outlet
The horizontal velocity check has no equivalent in a circular tank — it is the reason a
rectangular clarifier can fail even when its SOR is textbook.
| Item | Value | Basis |
|---|
4Sludge balance & collection
The underflow must be able to carry away at least as much solids as arrives. If it
cannot, the blanket rises until it spills over the weir — the classic secondary-clarifier failure.
| Item | Value | Basis |
|---|
Operation envelope
| Item | Value | Basis |
|---|
5Instrument schedule
The sludge blanket level is the single most useful measurement on a secondary clarifier
— and the one most often missing.
| Point | Instrument | Why here |
|---|
Quote the clarifier instruments at factory price
Blanket level, effluent turbidity, MLSS and RAS flow — all mappable to our catalogue and supplied at the manufacturer's ex-works price (our margin is the export rebate, not a markup on the device).
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Sources & parameter basis
| [1] | METCALF & EDDY / EPA — secondary clarifier: peak SOR 30–50 m³/m²·d, average SOR 15–30, SLR 100–250 kg MLSS/m²·d (typ. 120–200), side water depth 3–4.5 m, HRT 2–4 h, RAS 0.5–1.5×, minimum 2 tanks. |
| [2] | Underflow concentration from SVI: CRAS ≈ 10⁶/SVI mg/L (valid SVI 80–150); equivalently RAS ≈ MLSS × 1000/SVI. |
| [3] | Rectangular geometry: L:W 3:1 to 6:1; horizontal velocity limited to about 1.0–2.0 m/min at peak flow to avoid scouring the settled blanket. |
| [4] | Weir loading: 125–250 m³/m·d at average flow, up to 375 m³/m·d at peak. Side-wall weirs give 2L of weir length per tank, end weirs give W. |
| [5] | Chain-and-flight scraper: 0.3–1.2 m/min; flight spacing 3 m; the return run should clear the collected sludge well inside its detention time. |
Full derivation and worked example: Rectangular-Secondary-Calculation-Sheet.md.
Try switching the weirs from both side walls to end-weir-only — you will watch the weir load roughly
quadruple and the design stop working. That is why rectangular tanks run their effluent launders along
the long walls.
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Engineer's FAQ
Frequently asked about rectangular secondary clarifiers
How do I calculate the side water depth of a rectangular secondary clarifier?
Side water depth (SWD) = effective clarifier volume ÷ (length × width). For conventional rectangular secondary clarifiers it is normally 3.0–4.5 m. Depth sets the solids residence time and sludge-blanket stability — too shallow invites short-circuiting, too deep raises civil cost.
What is a typical side water depth for a secondary clarifier?
Rectangular units run 3.0–4.5 m; a few high-rate designs reach 5 m. The chosen SWD balances hydraulic retention, sludge-blanket control and civil cost against the surface overflow rate your effluent limit demands.
How does secondary clarifier design affect effluent quality?
Effluent clarity is governed by surface overflow rate and weir loading more than by depth alone. Size those against your peak flow, then confirm the geometry with a full design check.
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- Lamella Secondary ClarifierInclined-plate high-rate clarification
- MBR Design CalculatorMembrane flux, aeration, permeate quality
- Equalization Basin (Bế điều hòa)Flow & load equalization sizing
