505 MLD

Average design flow modelled (baseline case)

1.91 M cells

Polyhedral mesh, refined at screens and outlet chamber

Porous jump

Screen losses calibrated to manufacturer data

DPM

Particle tracking to locate sediment-prone zones

The challenge

Even flow across parallel screening channels

Raw sewage arrives through gravity sewers and must split evenly between parallel trains of coarse and fine screens. Uneven flow overloads some screens and leaves others under-used, and slow zones collect grit and solids. The client needed to know how the existing arrangement performs and where it should be improved.

CFD flow domain of the screening building
Flow domain: inlet sewers, distribution chamber, screening channels and outlet chamber

Our approach

CFD methodology

  1. Full hydraulic path modelled: inlet and outlet sewers, distribution and outlet chambers, screening channels and guide walls
  2. Half-domain model with a symmetry plane, where the layout allowed, to save about 50% of the cells
  3. Pressure-based steady-state solver with k–ω SST turbulence and gravity
  4. Coarse and fine screens represented by porous-jump zones calibrated to the manufacturer’s head-loss data, and validated on a test channel first
  5. Polyhedral mesh of 1.91 million cells, refined around screens, junctions and the outlet chamber
  6. Suspended solids at 100 mg/L tracked with the Discrete Phase Model to find where particles linger and settle
Polyhedral CFD mesh of the screening building
Polyhedral volume mesh

Results

Key results

Velocity contours through the screening channels
Velocity magnitude through the facility
Velocity vectors showing recirculation
Velocity vectors: recirculation in the outlet chamber
Particle tracks coloured by residence time
Particle tracks coloured by residence time: long residence means settling risk

Key findings

  • The design flow arrives smoothly, with no separation upstream, and turns cleanly around the guide walls.
  • Screen head loss is reproduced within the manufacturer’s range, and both trains stay in service at design flow.
  • Flow is biased toward the central channel, so the side channels are under-loaded and the screens unevenly used.
  • Recirculation in the outlet chamber and vortices at the splitter walls create low-velocity zones where particles linger longest, the main sediment risk.
  • Recommendation: add baffling or rearrange the internal channels to even out the flow, and inspect and clean the outlet chamber regularly.

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