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FINAL REPORT - Grand River Conservation Authority

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<strong>Grand</strong> <strong>River</strong> Watershed-Wide Wastewater Optimization Pilot Project<br />

Figure 13: PPG for Example CAS<br />

Design 4500 Annual average 4100<br />

0 1,000 2,000 3,000 4,000 5,000 6,000 7,000<br />

Primary Settler SOR<br />

(24 m3/m2.d)<br />

3,770<br />

Aeration HRT<br />

(6 h)<br />

BOD5 Loading<br />

(0.5 kg PE BOD5/d per m3)<br />

O2 Availability<br />

[1.0 kg O2 per kg (BOD5 + 4.6 TKN]<br />

Sec. Clar. SOR<br />

(24 m3/m2.d)<br />

Chlorine Contact Basin<br />

(30 min)<br />

6,000<br />

5,245<br />

4,897<br />

5,429<br />

4,800<br />

Anerobic Digester<br />

(40 d & 2.5%-4.0%)<br />

2,713<br />

1,628<br />

Sludge Disposal<br />

("on demand")<br />

4,100<br />

Annual Average Flows (m 3 /d)<br />

Performance Potential Graphs were completed for 12 WWTPs in the <strong>Grand</strong> <strong>River</strong><br />

watershed as a result of the workshop and previous activities in the City of Guelph<br />

and Haldimand County. The results are summarized in Table 10 below.<br />

Table 10: Summary of Major Unit Process Evaluation for<br />

<strong>Grand</strong> <strong>River</strong> Watershed WWTPs<br />

WWTP Q/Q d * Rating Most Limiting Unit Process<br />

A 52% To be determined To be determined<br />

B 51% capable O 2 availability<br />

C 77% not capable aerobic digester HRT<br />

D 56% capable liquid retention time<br />

E 48% capable secondary clarifier SOR<br />

F 47% capable Chorine contact basin<br />

G 72% capable To be determined<br />

H 45% capable aerobic digester HRT<br />

I 54% capable BOD loading rate<br />

J 68% capable O 2 availability<br />

K 64% not capable anaerobic digester HRT<br />

L 81% not capable BOD loading rate and aeration HRT<br />

M 53% not capable anaerobic digester HRT<br />

N 63% capable BOD loading rate<br />

Notes: * Q/Q d is the current annual average flow divided by the WWTP’s nominal design<br />

flow, expressed as a percentage.<br />

36 | Page

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