Granular media · service and backwash

Filter service, series & backwash calculator

Choose a controlled service rate and a controlled backwash target. Then test single, parallel or series arrangements—including the temporary loading when one series vessel backwashes through another.

Two media filters showing service and expanded-bed backwash states
1 · Vessel arrangement
2 · Media and controlled rates

Controlled duty point

Coconut-shell activated carbon

Q = rate × A
Backwash flow per vessel7.14m³/h31.4 GPM · 1.19 m³ backwash-step water
Actual service loading4.20 GPM/ft²10.28 m/h
Controlled service limit3.57 m³/h
Series transient upstream10.00 GPM/ft²2.38× normal loading

Action:

What to do when flows do not match

Control the flow; do not average an impossible range.

Set the service limit with a flow controller, VFD or balancing valve, or add vessel area in parallel. Set backwash with the correct DLFC/orifice, VFD or control valve. Excess backwash can lose media; insufficient backwash leaves the bed dirty.

Area = π × internal diameter² ÷ 4Service limit = selected service rate × online parallel areaBackwash flow = selected backwash rate × one vessel areaWash volume = backwash flow × time

Pump-curve checkpoint

The pump must meet one exact target at the real head.

Plot the selected backwash flow against total dynamic head: static lift, pipe/fittings, valve or DLFC, distributor/underdrain, dirty bed and drain backpressure. Verify the pump/system-curve intersection, runout, NPSH and valve capacity.

  1. Use the exact media expansion curve at actual temperature.
  2. Backwash one vessel at a time unless explicitly designed otherwise.
  3. Prefer a treated-water header or tank for series systems.

Series is not parallel

Two series filters still carry the same 3 m³/h.

Series stages add treatment barriers and pressure loss, not flow capacity. If downstream backwash water must pass through the upstream vessel, that upstream vessel temporarily sees the downstream backwash flow as service flow. This can be acceptable briefly only after checking dirty-bed pressure loss, valve/internals, available inlet pressure and water suitability.

Worked example · 3 m³/h

24″ GAC stage × 2 in series

At 5 GPM/ft², the theoretical diameter is about 22 in, so a 24 in vessel is hydraulically conservative only. Its actual loading at 3 m³/h is 4.20 GPM/ft². GAC backwash at the selected 10 GPM/ft² is 7.14 m³/h and uses 1.19 m³ in 10 minutes. Passing that through the upstream 24 in vessel gives 10 GPM/ft²—2.38× normal service loading. Final GAC bed volume must still meet EBCT, contaminant load and breakthrough criteria.

Check the assumptions

Method and primary references

The equations are shown so the result can be checked. Product data and site conditions still govern final selection.

From answer to equipment

Bring the duty point, not just a product name.

Watermart can check the calculation against the actual water analysis, pressure, valve, pump and installation constraints.

Discuss this calculation

Educational preliminary calculation—not a stamped design, quotation, or treatment-performance guarantee.

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