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Methodology for pAS application

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management in wastewater treatment plants

3.4.4 Methodology for pAS application

The first step of PAS application is the definition of the objectives and of the assessment criteria for a given WWTP or a group of WWTPs. The PIs must then be selected and calculated accordingly, and analysed against the references values.

Further insights may require the use of complementary PIs.

The next step is the selection and calculation of PXs to complement the information provided by the homologous PIs. The latter assess the overall performance in the

2Applicable to conventional (with or without sludge return) and enhanced primary sedimentation.

3Variables applicable to several AS variants: complete mix; plug flow (conventional, extended aeration); oxidation ditch (C removal, C + N removal); A/O; MLE; Bardenpho (4-stage, 5-stage); A2/O;

UCT; VIP; SBR (C removal), SBR (C + N removal) and SBR (C + N + P removal). The performance functions are AS-type specific.

4Except for SBR.

5Variables applicable to different filter packing (mono and dual media) and height; performance functions are filter-type specific.

6Net treatment capacity accounts for the water filtered minus the water spent for cleaning and the filtration time plus the cleaning time.

7Excluding the g-force, the variables listed are applicable to gravity, dissolved air flotation, gravity belt and rotary drum thickening. The performance functions are thickener-type specific.

8Applicable only to anaerobic digestion.

9Applicable to centrifuge, belt filter press, recessed-plate filter press and sludge drying beds. The performance functions are dewatering-type specific.

10Applicable only to centrifuge.

table 3.5 State-variables relevant for assessing the WWTP energy performance (adapted from Silva et al. 2013) (Continued).

treatment unit or step (type)

State-variables relevant for energy performance [units]

UV disinfection UV dose [mJ/cm2]

Unit energy consumption [kWh/m3]

Thickening7 Daily operating hours of mechanical thickeners [hours/day]

Relative centrifugal force (g-force) [× g]

Unit energy consumption [kWh/m3] Stabilization

(aerobic and anaerobic digestion)

Solids retention time (without recirculation) [d]

Biogas production8 [m3/kg converted VSS]

Production of energy from biogas [kWh/m3] Unit energy consumption [kWh/m3]

Dewatering9 Daily operating hours [hours/day]

Rotational speed10 [rpm]

Relative centrifugal force (g-force)10 [× g]

Unit energy consumption [kWh/m3]

assessment period (usually, a calendar year) and the PXs assess ‘where’ (unit operations/processes and equipment) and ‘when’ the performance did satisfy or fail the pre-established objectives and the distance that remains to achieve these targets (Silva et al. 2014a), enabling the identification of improvement actions.

As introduced earlier, prior to WWTP energy efficiency one should verify the plant effectiveness and reliability, that is, the compliance over time with the quality requirements of the treated water (Silva et al. 2014a). One may then select the parameters and unit operations or processes for which one intends to assess and optimise the removal efficiency to enhance the treatment reliability (Silva et al. 2014b).

The continuous improvement of WWTP performance requires the verification and, eventually, the (re)definition of objectives and (re)selection of the corresponding PIs and PXs, which restarts the PDCA cycle of PAS application (Figure 3.10).

Figure 3.10 PDCA methodology for the continuous improvement of WWTP energy performance.

3.5 rEFErEncES

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