Yorkshire WWTP: 11% Less Polymer in Dewatering

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Key results
11% centrifuge polymer cut
Lower centrifuge stress
Output quality maintained

Case Study from HYDROPATH

Sludge dewatering polymer reduction on a centrifuge

Sludge dewatering polymer reduction was the goal at a Yorkshire wastewater treatment works dosing heavily with polymer on its dewatering centrifuges. The works could not simply dose less: cutting polymer risked floc loss, cake dryness had to be held near 21% to feed the thermal hydrolysis plant, and centrate quality had to stay within process limits. During an October to November 2018 trial, one HydroFLOW® i160 was fitted to the incoming sludge feed pipe before polymer injection on centrifuge 3. Polymer dosing fell by 11%, with cake dryness and centrate quality both holding and no change to the downstream process.

The Challenges

  • Sludge dewatering polymer reduction was needed, with high dosing on the centrifuges
  • Any cut in polymer dosing risked floc loss
  • Cake dryness had to stay near 21% to feed the thermal hydrolysis plant (THP)
  • Centrate quality had to remain within process limits
  • Any change had to be proven on a live centrifuge

The Solution

  • Unit installed: one HydroFLOW® i160
  • Installation point: incoming sludge feed pipe, before polymer injection on centrifuge 3
  • Trial: October to November 2018 on a live centrifuge

The works needed sludge dewatering polymer reduction without upsetting a live centrifuge, so the unit was fitted to the sludge feed pipe on centrifuge 3, ahead of polymer injection. The signal improves flocculation, so polymer demand falls. The polymer saving was then measured against the two constraints: cake dryness near 21% and centrate quality within process limits.

Key Outcomes

R

Polymer use cut 11% on matched centrifuge runs

R

Cake dryness and centrate TSS within limits

R

Higher differential RPM, lower centrifuge stress

R

Switching unit off caused rapid floc loss

Independent Verification

All results in this study were measured and verified by third-party facilities managers and technical staff.

Summary

The trial cut polymer by 11% while cake dryness held near 21% and centrate stayed within limits. Polymer is usually the largest chemical cost in a dewatering plant, and cutting it without losing cake dryness is the constraint that defeats most attempts. Here the saving came without touching the centrifuge settings or the THP feed specification, and with no change to the downstream process. For any works feeding thermal hydrolysis, this trial is the model to follow.

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