How to calculate the settling area and media volume you need, why the installation angle matters, and how to specify PP, FRP or stainless steel for your tank — using the parameters we actually publish on the product page.

Prefer to run the numbers yourself? Use the online tube settler media calculator.
Tube settler media is sized on surface loading rate, not on tank volume. Get the settling area right and the rest of the design follows.
Take the peak hydraulic flow through the clarifier, in m³/h. Use peak flow, not average — tube settlers are most often undersized because the design was based on daily average.
For tube settler media we publish a hydraulic load of 3–5 t/m²·h (equivalent to 3–5 m³/m²·h). Fast-settling mineral solids suit the higher end; light biological floc needs the lower end.
Required settling area A = Q ÷ SLR. A 100 m³/h flow at 4 m³/m²·h needs about 25 m² of projected settling area.
| Design flow Q | 100 m³/h (peak) |
| Surface loading rate SLR | 4 m³/m²·h |
| Required settling area A = Q ÷ SLR | 25 m² |
| Stack height | 4.5 m |
| Indicative media volume A × height | ≈ 112 m³ |
| Check: velocity inside the tubes | 2.5 – 3.0 mm/s (design V₀) |
Media volume is normally quoted in m³, so the final figure you send to a supplier is the volume plus the pore size and material. The exact module count depends on the installed footprint and how the modules are cut around weirs and launders — that is confirmed per project rather than assumed from a catalogue.
The installation angle is the single most common specification question from engineers in the UK and Europe, and it is not a free choice.
Our modules are installed at 60° from horizontal. Steeper angles cost effective settling area; shallower angles stop sludge sliding down the tube wall.
The tube wall has to be steep enough that settled solids keep moving back down to the sludge zone. If they stall, the tube blocks and the module has to be taken out and washed.
Because the modules are inclined, the projected settling area you gain is not the same as the module's physical footprint. This is why the calculation above works in settling area first, and converts to media volume second.
Material of construction (MOC) decides both the chemical duty and the service life. All three options below are published specifications.
| Material | Pore sizes | Thickness | Surface area | Porosity | Density |
|---|---|---|---|---|---|
| PP (polypropylene) | Φ25 / 35 / 50 / 80 | 0.5 – 0.8 mm | 62 – 200 m²/m³ | 93 – 97% | 22.8 – 46 kg/m³ |
| FRP (glass fibre) | Φ25 – 60 | 0.5 mm | 99 – 236 m²/m³ | 93 – 97% | 42 – 95 kg/m³ |
| Stainless steel (custom) | Φ25 / 35 / 50 / 60 / 80 / 90 | 0.5 – 0.8 mm | 62 – 236 m²/m³ | 93 – 97% | On request |
The default choice. Service life is published as PP 3–4 years; co-polymer based media can extend that to 8–10 years in water.
Up to 236 m²/m³, so it packs more settling surface into the same tank volume when space is the constraint.
Stainless steel modules are built to order and go up to Φ90 mm. Density is quoted On request because it depends on the grade and wall thickness specified.
Tube settler modules are stacked to a published height and then fixed so they cannot float, shift or short-circuit.
Modules are stacked to a total height of 4–5 m. Below that the settling benefit drops away; above it the head loss and the support structure cost both rise.
Modules sit on a support frame and are restrained from above. Empty PP modules are light (22.8–46 kg/m³), so uplift and movement in a draining tank are a real failure mode if they are not tied down.
The most common use is not a new clarifier — it is an existing tank that needs more capacity without a bigger footprint. Modules are cut to suit the existing weirs, launders and sludge scrapers.
These are the published figures for our tube settler media — useful as a sanity check when you compare quotations.
| Handling capacity vs a flat basin | 3 – 5× |
| Handling capacity vs a shallow tank | 2 – 3× |
| COD removal | 85 – 90% |
| Organic load | 2000 – 5000 g/m³·d |
| Design velocity V₀ | 2.5 – 3.0 mm/s |
| Hydraulic load | 3 – 5 t/m²·h |
| Service life | PP 3–4 yrs; co-polymer up to 8–10 yrs |
| SKU / price | NWS-HXT series · On request |
Pore size trades surface area against blocking risk. Smaller pores (Φ25–35 mm) give more surface area per m³ and better removal of fine solids, but block sooner with fibrous or oily loads. Larger pores (Φ50–90 mm) stay clean longer and suit high-solids or desanding duty. Tell us your solids type and we will confirm the pore size.
Work out the settling area from your flow and surface loading rate (Step 1), then multiply by the stack height. Send us the flow rate, tank dimensions and target solids, and we will return a checked quantity.
Yes — it is common to use one material where the duty is aggressive and another elsewhere. Because modules have to be cut to the same stack height, it is worth fixing the material schedule before the tank is measured.
Price depends on material, pore size, sheet thickness, total volume, packaging and destination port. Because those vary per project we confirm the specification first and quote against it rather than publishing a list price that would not apply to your case.
Both are inclined settling media. Tube settler media uses hexagonal tubes; lamella plate media uses flat plates. The choice usually comes down to the duty and what the tank can accept. See the inclined plate media page for the plate version.
Municipal wastewater, industrial effluent, inlet desanding, oil separation, tailings thickening and old-tank retrofits. See the product page for the full application list.