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2019 ANNUAL SUMMARY REPORT

Amended Environmental Compliance Approval

Number 6245-AB6HDR

The 2019 WPCP Summary Report was prepared by:

Holly Grant Compliance Coordinator

Reviewed by: Ted Joynt “Acting” Overall Responsible Operator

Corporation of the Township of Cramahe Village of Colborne Wastewater Treatment Plant Performance Report 2019

Executive Summary

The enclosed Annual Summary report is prepared in accordance with Amended

Environmental Compliance Approval (ECA) # 6245-AB6HDR Condition 9 Reporting

subsection (5) for the Township of Cramahe (Operating Authority) Village of Colborne Water

Pollution Control Plant (WPCP) for submission to the Ministry of Environment Conservation

& Parks (MECP) no later than March 31, 2020. An extension by the MECP was granted until

April 13, 2020, due to COVID-19.

The secondary purpose of this 2019 Summary Report is to keep the Operating Authority,

Owner (Council) informed regarding the general operation, maintenance and facility

compliance regarding solids and liquid handling and disposal as per the ECA.

Each year it is a requirement that the owner prepares and submits an annual summary

report for the previous calendar year and must contain the following information:

A. A summary and interpretation of all monitoring data and a comparison to the

effluent limits outlined in Condition 6, including an overview of the success and

adequacy of the Works;

B. A description of any operating problems encountered and corrective actions

taken;

C. A summary of all maintenance carried out on any major structure, equipment,

apparatus, mechanism or thing forming part of the Works;

D. A summary of any effluent quality assurance or control measures undertaken in

the reporting period;

E. A summary of the calibration and maintenance carried out on all effluent

monitoring equipment; and

F. A description of efforts made and results achieved in meeting effluent objectives

listed Condition 5.

G. A tabulation of quantity of sludge generated in the reporting period, an outline of

anticipated quantities to be generated in the next reporting period and a summary

of the locations to where the sludge was disposed;

H. A summary of any complaints received during the reporting period and any steps

taken to address the complaints;

I. A summary of all by-pass, spill or abnormal discharge events;

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J. A copy of all notices of Modifications submitted to the Water Supervisor as a result

of Schedule B, Section 1, with a status report on the implementation of each

modification;

K. A report summarizing all modifications completed as a result of Schedule B

Section 3; and

L. Any other information the Water Supervisor requires from time to time.

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Referencing Information

Colborne Wastewater Treatment Plant 2019 Performance Report

Owner and Operating Authority – Corporation of the Township of Cramahe

Environmental Compliance Approval – 6245-AB6HDR, August 8, 2016

Mailing Address – PO Box 357, Colborne, Ontario, K0K 1S0

Site Address - 1108 Ontario Street, Colborne, ON

Municipal Contact Phil Kelly, Operator-in-Charge Voice – (905) 355-2982 Email – [email protected]

Compliance Coordinator Holly Grant Voice – (905) 355-2821 Ext: 126 Email – [email protected]

Acting ORO Ted Joynt Cellular - 613-284-7290 Email - [email protected]

Works Number # 120000088

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mailto:[email protected]




Table of Contents

Contents Executive Summary .................................................................................................... 1

Table of Contents ....................................................................................................... 4

1. A summary and interpretation of all monitoring data and a comparison to the effluentlimits outlined in Condition 6, including an overview of the success and adequacy ofthe Works; ...................................................................................................... 6

2. Process Description ........................................................................................ 6

3. A description of any operating problems encountered and corrective actions taken; ................................................................................................................... 9

4. A summary of all maintenance carried out on any major structure, equipment,apparatus, mechanism or thing forming part of the Works; ................................. 10

5. A summary of any effluent quality assurance or control measures undertaken in thereporting period; ............................................................................................ 10

6. A summary of the calibration and maintenance carried out on all effluent monitoringequipment and; ............................................................................................. 11

7. A description of efforts made and results achieved in meeting effluent objectiveslisted Condition 5. .......................................................................................... 11

8. A tabulation of quantity of sludge generated in the reporting period, an outline ofanticipated quantities to be generated in the next reporting period and a summary ofthe locations to where the sludge was disposed; ................................................ 12

9. A summary of any complaints received during the reporting period and any stepstaken to address the complaints; ..................................................................... 12

10. A summary of all by-pass, spill or abnormal discharge events; .......................... 12

11. A copy of all notices of Modifications submitted to the Water Supervisor as a resultof Schedule B, Section 1, with a status report on the implementation of each modification. ................................................................................................. 12

12. A report summarizing all modifications completed as a result of Schedule B Section3. ................................................................................................................. 13

13. Any other information the Water Supervisor requires from time to time .............. 13

14. Summary .................................................................................................... 14

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APPENDICES

Appendix A – Environmental Compliance Approval #6245-AB6HDR

Appendix B – Monitoring Data and Comparison to Effluent Limits

Appendix C – Maintenance Records

Appendix D – MUMPS Report

Appendix E – Lethality Testing

Appendix F – Calibration Reports

Appendix G – Bypass Report

Appendix H – Operator Licenses

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1. A summary and interpretation of all monitoring data and a comparison to

the effluent limits outlined in Condition 6, including an overview of the

success and adequacy of the Works;

The Wastewater plant functioned and was maintained by means so that the

concentrations and waste loadings of material (CBOD5, TSS, TP, TKN, Total

Chlorine Residual, and E.coli) met all effluent parameters and did not exceed

limitations. The monthly average concentration and average loadings were all

within limits. The pH of the effluent was maintained within range of set

limitations at all times. Flows were well within the Design Flow Rate (based on

monthly averages) and the yearly average of all limits was well within the set

perimeters.

The results of the Total Phosphorus (TP) testing by SGS Canada Inc, for the

month of July indicated that the monthly average for TP exceeded the ECA limit of

0.70 mg/l. The monthly average was 1.16 mg/l. All other months did not

exceed the limits set out for the effluent discharged from the plant and the

effluent was continually disinfected to meet these limits.

See Appendix B

2. Process Description

The Colborne Wastewater Treatment Process is an extended aeration process.

Raw Sewage flows by gravity (there are no lift stations) to the plant where the

wastewater passes through a “Muffin Monster” (grinder) to comminute the

sewage. The sewage is then pumped to grit channels and thence flows by gravity

to an aeration basin followed by a clarifier. Aluminum Sulphate (coagulant) is

added between the aeration basin and the secondary clarifier where phosphorous

and solids removal occurs.

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The process treated sewage then flows to an effluent pumping station where

sodium hypochlorite (NaOCl) is added for disinfection. The sewage is then pumped

into a force main to a dechlorinating facility (using sodium metabisulphite

(Na2S2O5) located approximately 1.25 km south from the plant. From the

dechlorinating facility, final effluent flows to Lake Ontario.

There are two unique features in the plants design. The first being a peak flow

attenuation pond, to which raw sewage flows when it exceeds the designed

peak flow and then is directed by an overflow weir. As such there is virtually

no chance for a sewage bypass. The peak flow attenuation pond is emptied by

directing flow back into the plant for treatment once peak flows subside. The

second feature is a bio solids holding pond which has the capacity to hold

several years of sludge. This bio solids holding pond decants by gravity into

the peak flow attenuation pond.

The facility has an onsite waste Stabilization Pond with a capacity of 4000 m3

for the storage for waste activated sludge (WAS). WAS is discharged to this

Stabilization Pond where odors’ are controlled and the sludge is allowed to

stabilize so that land application can occur. Every 3 to 4 years this “sludge”

must be removed and land applied in order to make room for future sludge

buildup. Removal occurred in October 2016.

There are two composite samplers, one for raw wastewater and one for final

effluent. There are two final effluent sample points, one at the dechlorinating

facility and the second sampling point at Station 2 (final effluent), prior to

discharge to Lake Ontario.

The Water Pollution Control Plant (WPCP) is presently operating with a Supervisory

Control and Data Acquisition (SCADA) system. This system automates all of the

electrical, chemical and mechanical schemes, which work in combination to treat the

waste water. The SCADA system was updated in 2018, improving and allowing for

better collection, interpreting and trending of data. The upgrades involved the

installation of a new PLC control program (iFIX), along with new SCADA computers

and monitoring screens. As well, a new data historian reporting system was

installed (e-RIS) which allows for better control over plant data then the previous

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reporting system. The new system also includes complete redundancy to ensure

that should one SCADA computer fail, then the other can be used without loss of

data or plant control.

The SCADA system allows the operators to control, monitor, trend and report on

various aspects of water plant including:

• Influent pump station pump control,

• Aeration tank blower control,

• Groundwater pump station pump control,

• Alum injection system control,

• RAS / WAS pump & valve control,

• Scum pumping station pump control,

• Effluent pumping station pump control,

• Monitoring of various other alarms and process parameters,

The SCADA process control system, ultimately filters commands that control pumps,

process interlocks and alarms that alert operators when equipment malfunctions or

processes fail. The system also monitors and tracks large volumes of data that are

used for trending, process control and compliance reporting. The computers and

servers that make up the SCADA system operate 24/7 and are never shut down.

The dechlorinating facility includes dosing based on flow, which is likewise

monitored through the SCADA system.

Flows are measured by Parshall flumes, one Parshall flume is located immediately

upstream of the grit channels and one after the clarifier. There is an

electromagnetic flow meter located at the dechlorinating facility used for process

control to dose the dechlorinating agent and measure flow to Lake Ontario.

Emergency power is provided by an onsite generator capable of running the

facility with power to spare. This generator is exercised monthly to make sure it’s

always ready to supply power during a power outage. There is also a second

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generator located at the dechlorinating building should line power be effected at

that location.

3. A description of any operating problems encountered and corrective actions

taken;

Noncompliance for Total Phosphorous

Testing results of TP by SGS Canada Inc, for the month of July indicated that the

monthly average for TP exceeded the ECA limit of 0.70mg/l; the monthly average

was 1.16mg/l. On July 21st, an increase in the dosage of coagulant was made; the

intent was to bring the TP back into compliance. Compliance was confirmed in the

following weeks testing and it did lower the residual TP in the effluent stream. The

cause was thought to be attributed to lower flows into the plant, which may have

decreased the dilution factor in the raw wastewater.

Corrective Action

A review of the Raw Wastewater flows and of the TP Concentration in the Raw

Wastewater did not support lower flows into the plant, thereby causing a dilution.

Verification of the exceedance was not confirmed, however continued monitoring of

the residual TP in the effluent and adjustments were made to the coagulant as

required.

Influent and Outfall Samples Missed

The Raw Wastewater and Effluent Wastewater sample for the week of November 17th

was not sent to the Lab for testing and analysis. Terms and conditions Section 8 -

Monitoring and Recording were not adhered to. It was determined the courier had

not picked up the samples from the drop site. The samples were located and could

not be resent as they were outside the “holding time”. New samples were collected

and sent for testing.

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Corrective Action

Samples cannot be picked up at the plant as the courier times are hard for staff to

adhere to and entry to the plant can be restricted. To further reduce the risk of this

happening again, a procedure has been written and implemented. This will provide

better direction to staff and change the pickup site from the Keeler Centre to the

Town hall, as there is always someone there to assist and make sure samples are

picked up.

4. A summary of all maintenance carried out on any major structure, equipment, apparatus, mechanism or thing forming part of the Works;

No major equipment repairs were needed throughout the year. Routine

maintenance was carried out based on manufactures’ recommendations and as

needed. Electrical company replaced the Transfer Switch Gear in the Generator

Building.

See Appendix C

5. A summary of any effluent quality assurance or control measures

undertaken in the reporting period;

Quality control is monitored using the daily SCADA printouts and online

instrumentation location in the control room. Reviewing the laboratory results

when they are received, and routine activities such as manually checking sludge

depths add to the control measures taken. A daily and monthly report is

populated as data is entered into the SCADA system. The reports contain

conditional formatting which alerts the operator to any situations where the ECA

limits and objectives are exceeded.

Process changes are made based on an accredited laboratory results, in-house

testing and physical monitoring so as to achieve the best quality effluent.

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See Appendix – D - MUMPS - Municipal Utility Monitoring Program

See Appendix – E - Acute Lethality of Municipal Sewage Effluents

6. A summary of the calibration and maintenance carried out on all effluent

monitoring equipment and;

The plant flow meters were annually calibrated at the end May by Franklin Empire

Inc. Other instrumentation, such as pH meters are calibrated in-house prior to

each use.

See Appendix F - Calibration Reports for 2019

7. A description of efforts made and results achieved in meeting effluent

objectives listed Condition 5.

The plant effluent concentrations in terms of CBOD and Total Ammonia Nitrogen

(TAN) and Total Suspended Solids (TSS) and Total Phosphorous (TP) were all

within the required ECA limits for 2019. The limits for Total Chlorine Residual

were met. Data collected for 2019 shows that the extended aeration process

provided a high quality of effluent.

The nutrient loadings on the receiving body of water (Lake Ontario) were within

the criteria noted in the Environmental Compliance Approval #6245-AB6HDR.

A summary of the 2019 Operating Data is attached as Appendix B to this

report.

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8. A tabulation of quantity of sludge generated in the reporting period, an

outline of anticipated quantities to be generated in the next reporting period

and a summary of the locations to where the sludge was disposed;

In October of 2016 the “waste sludge” was removed from the waste stabilization

pond. We are estimating based on the sludge removed that approximately 700 to

800 cubic meters of wasted sludge accumulates every year. There was no sludge

removed or land applied in 2019. The quantity of sludge estimated to accumulate

in 2020 will be similar to what was generated in 2019.

9. A summary of any complaints received during the reporting period and any

steps taken to address the complaints;

No formal complaints were received in 2019 regarding the Wastewater Treatment

Plant.

10. A summary of all by-pass, spill or abnormal discharge events;

The plant includes a peak flow attenuation pond that permits discharge to the

pond during high flows, as such there were no plant bypass events or abnormal

discharges or spills during the year. Quarterly reports were submitted to the MECP

as per the ECA.

See Appendix G – Bypass Report

11. A copy of all notices of Modifications submitted to the Water Supervisor as

a result of Schedule B, Section 1, with a status report on the implementation

of each modification.

There were no modifications as a result of Schedule B, Section 1 of the ECA

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12. A report summarizing all modifications completed as a result of Schedule B

Section 3.

There were no modifications as a result of Schedule B, Section 3 of the ECA.

13. Any other information the Water Supervisor requires from time to time

All requests for operating information by the district MECP office were responded

to. A facility inspection of the WWTP was performed in September of 2019 by the

MECP. The inspection involved: A visual inspection of the extended aeration

process, conformation of documentation (log books), Standard Operating

Procedures, general & major maintenance, confirmation of hours spent at plant,

training & licensing and compliance with the ECA. An inspection of all buildings,

particularly the Bisulphate building, as this building was noted in the last

inspection for inadequate spill containment. The MECP completed the inspections

and a final report was distributed to the Medical Officer of Health, Conservation

Authority, as well as staff connected to the report and the CAO.

See Appendix H – Operators Licensing

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Summary

The Colborne WWTP operated with the highest intent of achieving compliance and

maintaining a rated capacity of 1,750 m3/d, for the conduction and treatment of

the Raw Wastewater and disposal of effluent to Lake Ontario. It is anticipated

that 2020 will bring added focus on flow control during high flow periods.

Significate infiltration and inflow (I&I) in the collection system are the main focus

of an implemented control group, to help find a solution and restore our capacity

for future development. This working group has been reviewing data obtained by

camera & smoke testing of our collection system, reviewing engineering reports

and connecting with experts and other Municipalities. Open Channel Flow meters

have been purchased and are being used to eliminate problematic areas within

the Collection System.

The SCADA system is supporting the WWTP and staff with a dynamic reporting

structure. Eramosa Engineering Inc. has provided training to staff and has

completed majority of staff requests for recording configurations. We have

almost eliminated all paper and spreadsheets that were used previously.

The township operators continue to strive to attain their required licensing levels

and meet all training expectations that are required.

If you have any questions or require clarification please do not hesitate to

contact Ted Joynt Acting ORO or myself, Holly Grant.

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Please refer to the Process Schematic drawing on the following page.

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Appendix A – Environmental Compliance Approval #6245-AB6HDR

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Appendix B – Monitoring Data and Comparison to Effluent Limits

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Parameter Unit Jan Feb Mar Apr May June July Aug Sep Oct Nov Decm3 m3 m3 m3 m3 m3 m3 m3 m3 m3 m3 m3 m3 bjectiv Limit

Maximum Effluent Flow(4) FIT330 Influent m3/d 2972.7 2,648.15 4,612.06 3,408.69 4,492.58 2,052.19 1,984.07 1,538.10 1,875.09 3,067.76 2,287.44 5,000.00 N/A N/A 2994.90Minimum Plant Effluent Flow (4) FIT330 Influent m3/d 1006.6 987.76 911.39 1,733.92 1,542.26 907.03 754.75 620.28 624.18 672.55 1,024.42 964.66 N/A N/A 979.15Average Plant Effluent Flow (4) FIT330 Influent m3/d 1510.3 1,285.47 1,755.42 2,209.22 2,415.24 1,302.58 1,112.39 710.37 899.67 1,009.43 1,228.66 1,601.66 N/A N/A 1420.03Peak Flow Rate FIT330 Influent m3/d 4455.00 4,921.00 4,996.00 4,861.00 5,831.00 2,661.00 2,461.00 5,975.00 3,609.00 4,553.00 3,207.00 5,000.00 N/A N/A 4377.50Total Plant Flow for the Month FIT330 Influent m3 46,819.80 35,993.10 54,418.10 66,276.70 74,872.44 39,077.33 34,484.01 22,021.37 26,990.13 31,292.29 36,859.91 45,211.94 N/A N/A 514,317.12

Maximum Effluent Flow(4) FIT615 Effluent m3/d 2,385.57 2,110.39 3,714.19 2,677.07 3,645.87 1,670.15 1,616.81 1,268.06 1,596.41 2,598.76 1,935.64 1,928.30 N/A N/A 2,262.27Minimum Plant Effluent Flow (4) FIT615 Effluent m3/d 832.19 811.10 741.88 1,294.34 1,201.21 742.70 0.00 520.43 523.60 525.80 857.32 832.68 N/A N/A 740.27Average Plant Effluent Flow (4) FIT615 Effluent m3/d 1,207.86 1,039.77 1,375.57 1,707.63 1,910.50 1,056.09 768.42 611.54 744.60 819.62 1,005.43 1,157.55 N/A N/A 1,117.05Peak Flow Rate FIT615 Effluent m3/d 3,840.00 4,240.00 4,189.00 5,413.00 5,413.00 2,703.00 4,945.00 3,472.00 3,546.00 4,910.00 3,002.00 3,213.00 N/A N/A 4,073.83Total Plant Flow FIT615 Effluent m3 37,443.50 29,113.10 42,642.00 51,228.82 59,225.56 31,682.56 27,882.00 18,957.79 22,337.99 25,408.27 30,162.76 35,884.00 N/A 1,750.00 1,128.68

411,968.34Secondary Treatment Bypasses m3/d 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 N/A N/A 0.00

Diversion flow to Cell 1 FIT100 Cell 1 m3/d 0.00 0.00 0.00 0.00 317.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 317.00

Raw Sewage BOD mg/L 95.67 155.25 112.75 108.00 61.00 106.00 71.50 104.00 109.00 96.00 115.20 170.00 f N/A 108.70Raw Sewage TSS mg/L 125.67 142.75 126.00 115.00 70.60 128.00 61.50 117.40 81.00 88.00 114.70 142.7 N/A N/A 109.44Raw Sewage TKN mg/L 23.60 24.40 22.80 24.73 16.24 28.43 25.78 35.96 32.68 27.00 30.50 30.28 N/A N/A 26.87Raw Sewage TP mg/L 3.40 3.46 3.38 3.47 2.29 3.37 3.58 3.78 2.94 2.65 3.14 3.02 N/A N/A 3.21Effluent CBOD mg/L 3.0 4.75 4.5 4.25 2.4 2.25 4.3 2.0 2.00 2.00 1.75 2.75 15.0 25 2.99Effluent CBOD Loading (4) kg/d 3.62 4.95 6.19 3.84 4.59 2.38 3.27 1.22 1.49 1.64 1.76 3.18 43.8 43.8 3.18Effluent TSS mg/L 6.50 18.25 12.8 11.75 10.0 7.00 5.8 6.0 8.00 6.40 5 8.75 15.0 25 8.85Effluent TSS Loading (4) kg/d 7.85 18.98 17.54 20.06 19.11 7.39 4.42 3.67 5.96 5.25 5.03 10.13 N/A 43.8 10.45Effluent NH3 and NH4 mg/L 0.10 0.125 0.10 0.10 0.12 0.10 0.15 0.16 0.12 0.10 0.10 0.10 2/4 4/8 N/AEffluent TP mg/L 0.17 0.520 0.50 0.26 0.27 0.59 1.16 0.54 0.16 0.13 0.07 0.10 0.40 0.70 0.37Effluent TP Loading (4) kg/d 0.20 0.540 0.69 0.44 0.51 0.62 0.89 0.33 0.12 0.10 0.07 0.11 N/A 1.2 0.39Effluent TC mg/L 0.01 0.02 0.02 0.02 0.01 0.00 0.01 0.00 0.00 0.01 0.01 0.01 0 0.02 0.01Effluent E. Coli CFU/100 mL63.40 2.00 1.75 24.50 2.40 6.50 30.60 82.00 0.64 80.40 10.50 4.50 100 200 N/AEffluent Lethality Trout % N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/AEffluent Lethality Dm % N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/AMax pH 7.70 8.20 7.8 7.80 8.10 8.20 7.8 7.8 7.60 8.90 7.60 7.70 6.0 / 9.5 6.0 / 9.5 7.93Min pH 7.00 7.10 7.4 7.50 7.4 7.70 7.70 6.4 7.30 7.50 7.40 7.50 6.0 / 9.5 6.0 / 9.5 7.33Temperature Celsius 8.50 7.60 7.50 8.70 10.80 13.90 16.60 19.30 18.70 16.40 13.20 10.70 12.66Field pH 7.50 7.60 7.50 7.60 7.70 7.90 7.10 7.40 7.70 7.50 7.60 6.0 / 9.5 6.0 / 9.5 7.55Colour Scheme

Meets Objective or within design parametersMeets LimitsExceeds LimitRan to Pond

Notes The value listed is the design flow. There is not limit set in the Current ECA(1) The greater number applies Nov 1 to Apr 30(2) The ECA sets requirments if lethality is detected. The ECA provides that after eight (8) consecutive results with no lethality sampling can be reduced to annually.(3) Note flow meters are calibrated at +/- 15% as such flows and loadings vary within this range ECA section 8 (9) (4) ECA Number 6245-AB6HDR dated August 8, 2016

NOTE: Final Flows (average)for June through August are an estimate due to faulty flow meter FIT 615 finalAbbreviations

Dm Daphnia magna NO No set objectivekg/d kilograms per day NS Not sampledm3/d cubic metres per day TAN Total Ammonia Nitrogenmg/L milligrams per Litre TP Total PhosphorousNA Not Applicable TSS Total Suspened SolidsND Non Detect based on an average of <0.01 mg/L

ECA PARAMETERS

Colborne Water Pollution Control Plant 2019 Annual Results

ECA (5) Annual Avg C bi FIT330 INFLUENT FLOWS

FIT615 EFFLUENT FLOWS

DIVERSION FLOW TO CELL 1

Total Flow


Appendix C – Maintenance Records

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Date Equipment Company Operator Work CompletedJanuary 3, 2019 Generator Rowley Electric Ted Monthly check of Generators January 3, 2019 Hose Clamp Ted Change hose clamp on P612 - discharge hoseJanuary 11, 2019 Hypo Pump Phil Leak detected at hypo pump - repairedJanuary 14, 2019 Hypo Pump Phil Minor Leak in Hypo Room - fitting repair - require new panel/re-doneJanuary 15, 2019 Sludge Conveyor Andrew Breaking up ice formation to prevent flytes from breakingJanuary 16, 2019 Hypo Pump Phil Leak detected at hypo pump - repairedJanuary 16, 2019 Sludge Conveyor Andrew Breaking up ice formation to prevent flytes from breakingJanuary 17, 2019 Hypo Pumps Franklin Empire Ted Wayne Harrison in to check wiring for new Hypo Control panel January 22, 2019 Alarm Phil Alarm - Chain & Flights - acknowledeged AlarmJanuary 27, 2019 Sludge Conveyor Phil Breaking up ice formation to prevent flytes from breaking, cross collctor also has ice build upJanuary 31, 2019 Generator Rowley Electric Ted Monthly check of Generators

January 31, 2019 Sludge Conveyor Phil Breaking up ice formation to prevent flytes from breaking, cross collctor also has ice build up, this is occuring 2 or 3 times a day

January 31, 2019 Cross Collector Ted & Phil Cross collctor ice build up and shut off. Phil poured hot water on long collector tensioner and is now running.

February 1, 2019 Drive Gear Andrew Breaking up ice formation February 4, 2019 Scum Trap Andrew Missing bolt from handle on Scum Trap - replaced and fixed

February 5, 2019 Hypo Pump Rowely Electric Andrew Small leak in hypo pump P612 - called Dan Rawley to unhook pump. Scum pump and effluent pump P730 sent to Branch Electric for repair.

February 7, 2019 Sludge Conveyor Andrew Breaking up ice formation to prevent flytes from breaking, cross collctor also has ice build upFebruary 13, 2019 Ice Build Up Phil Clean and cleared ice and snow from FlumeFebruary 19, 2019 Drive Gear Andrew Breaking up ice formation February 25, 2019 Drive Gear Andrew Breaking up ice formation February 26, 2019 Drive Gear Andrew Breaking up ice formation February 27, 2019 Generator Rowley Electric Andrew Monthly check of Generators February 27, 2019 Drive Gear Andrew Breaking up ice formation

April 2, 2019 Hypo Control Panel Franklin Empire Ted & PhilChange over the Hypo control panel. Dan Rowely on site for electrical. P611 & P612 pumps have been disconected and wired directly to the pump. SCADA still on and linked Calibrated the pH meter HQ411d

April 3, 2019 Hypo Control Panel Bryant Plumbing Phil Discuss plumbing for Hypo Control panel and repairs.April 11, 2019 Hypo Control Panel Rowley Electric Ted Working on Hypo Control panel April 15, 2019 Effluent Well Rowley Electric Phil Debris wound through pump and float in Effluent well. Corrected and working May 22, 2019 Effluent pump Rowley Electric Andrew & Phil Installed rebuilt effluent pump. P720 pumpMay 29, 2019 Hypo Pumps Bryant Plumbing Phil Working on hypo pumps and new feed system May 30, 2019 Effluent pump Rowley Electric Andrew & Phil Working on effluent pumps & wiring issues June 3, 2019 Scum Trap Phil Emptied scum trapJune 12, 2019 Generator Rowley Electric Phil Repairing generator transfer switch June 12, 2019 Collection system Quintie Sewer Phil Flushing and camering of collection systemJune 17, 2019 Collection system Quintie Sewer Phil Flushing and camering of collection systemJune 26, 2019 Scum pump Phil Issues with scum transfer pump - investigating June 26, 2019 Scum pump Phil More issues with scum pumped - clogged with grease - removed and working.June 27, 2019 Spot check Andrew Cleaned, flights, gears, chainsJune 28, 2019 SCADA Eramosa Redeploy reporting system having programming issues, rerunning reports that did not print outJuly 1, 2019 Scum Wet Well Quintie Sewer Phil & Andrew Quinte Sewer onsite to clean out the scum wet well.July 3, 2019 Scum Pump Phil Scum pump pulled due to clogging cleaned reinstalledJuly 12, 2019 Bio Tank Andrew Bisulphate tank refilled

July 15, 2019 SCADA Eramosa Ted & Phil Problem with RACO dialer, Telezon contacted, will be making repair to the phone line. Hypo pump leak repaired, new fitting.

July 16, 2019 Phone Line Telezon Phil Telezon repaired phone line

July 18, 2019 Sludge Ted & Phil Started draining Cell 1 to lower overall levels. Removing standing water over sludge blanket. Increased sludge wasting cycles to waste more sludge, also increase coagulant dosage to 60 mg/l from 40 mg/l to help reduce total phosphorous content

July 19, 2019 Scum Trap Phil Scum trap pumped

July 20, 2019 Phone Line Bell/Telezon Phil & Ted Phone line down between Bisulphate building and Plant, this resulted in no remote control from SCADA, This communication issues required more monitoring as signal back to plant interrupted.

July 21, 2019 Bio Tank Phil Visual check on Bisulphate, building and pumps, flow registering on PLC but not on SCADA. Monitoring through VNC, Bisulphate check again visual in afternoon

July 22, 2019 Phone Line Phil Phone line still down between Bisulphate and control room still requiring visual checks

July 23, 2019 SCADA Eramosa Phil Shane Carney onsite from Eramosa to work on SCADA issues resolved. Bell Canada tech onsite checking phone line for fault, issues not on Bell equipment. Telezon to attend

July 24, 2019 Phone Line Telezon Phil Telezon onsite to repair circuit issues at Bisulphate building. Continuing to drain Cell 1 lower.July 25, 2019 Hypo Pumps Phil Flows diverted to pond while plumbing fittings/lines being installed on Hypo pumpsJuly 26, 2019 Hypo Pumps Phil Debris found inside Hypo pump, cleaned and placed back in service, switched flows back to plant

July 29, 2019 Claifier Phil Cell 1 opened to continue draining to lower level. Coagulant dosage increased to 70 mg/l from 40 mg/l. Lab results indicating Total Phosphorous still increasing. Clarifier washed down, trash screen cleaned

August 6, 2019 Genorator Rowley Electric Phil Hydro out - genorator hard to start. Changed batteries - all good August 12, 2019 Genorator Rowley Electric Phil Working on genorator August 25, 2019 Collection system Quintie Sewer Phil Identifiy influtration in system, Quintie on site to help determine issues and find solutionAugust 28, 2019 pH meter Ted Calibrated pH meter bench September 5, 2019 Hypo System Rowley Electrical and Franklin Empire Phil Both contractors onsite to work on new Hypo panelSeptember 5, 2019 Hypo Pump Rowley Electric & Franklin Empire Ted & Phil Wiring for hypo pumps and control panel September 6, 2019 Cell 1 Phil Starting to drain Cell 1 to lower volume of wastewater this will contiue for several daysSeptember 9, 2019 Clarifier Andrew Replace shear pin in chain and flightSeptember 18, 2019 Cell 1 Phil and Andrew Moving sludge to the sides of the CellSeptember 18, 2019 Sludge pond Phil Cleaning sluge from cell 1 and moving into cell 2 September 19, 2019 Genset Rowley Electric Phil Testing GensetSeptember 20, 2019 Cell 1 Phil and Andrew Moving sludge to the sides of the CellOctober 15, 2019 P611 Hypo system TJ Pump stopped working fuse 170 blew replaced fuse and restarted pumpOctober 15, 2019 Cell 1 Phil Moving sludge to the sides of the CellOctober 24, 2019 Collection System Pulling MH covers checkcing collection system flowsOctober 28, 2019 Effluent pumps P210 showing leak alarm investigate issueOctober 31, 2019 Effluent pumps Rowley Electric Removing P210 so it can be sent away for repairsNovember 1, 2019 Franklin electric Franklin onsite to trouble shoot Hypo pump P611November 12, 2019 collection System Phil Inspecting flows in systemNovember 18, 2019 Generators Rowley Electric Phil Testing gensetsNovember 21, 2019 SCADA TJ SCADA 2 screen went black rebooted and running againNovember 25, 2019 P210 Phil Pump shipped to FlygtDecember 6, 2019 Scum pit Quinte sewer Cleaned pit December 19, 2019 SCADA Eramosa and Franklin Empire Both contractors working on issues with P112

MAINTENANCE 2019 WWTP


Appendix D – 2019 MUMPS REPORTS

Page 20

Ministry of the Environment Municipal Utility Monitoring Program (MUMP) R1

Mechanical Plants Project Name Colborne Wastewater Treatment Plant Mailing Address Unit No.

Street No. 1

Street Name Toronto Street

PO Box 357

Municipality/City/Town Colborne

Province ON

Postal Code K0K 1S0

Operating Authority The Corporation of the Township of Cramahe Mailing Address Unit No.

Street No.

Street Name Same As Above

PO Box

Municipality/City/Town

Province

Postal Code

File No.

Works Number Data Period

Days

Discharge Type

Update Code Month Year 4 6 1 2 0 0 0 0 0 8 8 0 1 19 3 1 2 R 1 2 3 11 16 19 20 21 22 80

C.P. 0 1 FLOWS Parameter Code Dec Monthly Results

12 13 Total Flow (103m3 ) 5 0 0 1 0 3 3 7 . 4 4 3 Average Daily Flow (103m3/d) 5 0 0 1 5 3 1 . 2 0 7 Maximum Daily Flow (103m3/d) 5 0 0 2 0 3 2 . 3 8 5 30 34 35 38 46

2 6 BYPASS No. of Occurrences 12 13 Plant Bypass Volume (103m3) 5 0 0 2 6

3 . Duration (hrs) 8 0 5 6 3 1 . Secondary Bypass Volume (103m3) 5 0 0 4 0 3 . Duration (hrs) 8 0 5 6 5 1 .

30 34 35 38

0 3 RAW SEWAGE No. of Samples 12 13 BOD5 (mg/L) 0 0 0 0 1

0 9 5 5 Suspended Solids (mg/L) 0 0 0 0 6 0 1 2 8 5 TKN (mg/L) 0 0 0 2 0 2 2 3 . 6 5 Total Phosphorous (mg/L) 0 0 0 3 3 1 3 . 4 5

30 34 35 38

0 4 FINAL EFFLUENT 12 13 BOD5

(mg/L) 0 0 0 0 1

1 3 . 0 5

Suspended Solids (mg/L) 0 0 0 0 6 1 8 . 4 5 Ammonia + Ammonium (mg/L) 0 0 0 1 9 2 0 . 1 5 TKN (mg/L) 0 0 0 2 0 2 . 0 Total Phosphorous (mg/L) 0 0 0 3 3 2 0 . 3 0 5

(Representative of Final Discharge) 30 34 35 38

0 7 DISINFECTION 12 13 Chlorine Used (kg as Cl2) 5 0 3 2 0

1 2 3 4 . 6

Chlorine Dosage (mg/L as Cl2) 8 0 4 1 0 1 6 . 2 Chlorine Residual (mg/L as Cl2) 8 0 4 2 0 1 0 . 0 1 0 5

(Representative of Final Discharge) 30 34 35 38 48 51 dd

Operator Telephone Number 905-355-2982

Email Address [email protected] / [email protected]/[email protected] Comments

Return completed form to:

1. Environmental Monitoring and Reporting Branch, MOE, at [email protected] AND 2. Your Environmental Officer at your local District/Area MOE Office. (Find your local MOE office: http://www.ene.gov.on.ca/environment) 2062 (2011/03) © Queen’s Printer for Ontario, 2011 Page 1 of 2


http://www.ene.gov.on.ca/environment



Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0

Operating Authority The Corporation of The Township of Cramahe Mailing Address Unit No.

Street No.

Street Name Same as above

PO Box


Province

Postal Code

File No.


Days

Discharge Type


C.P. RAW SEWAGE 3 6 Parameter Unit Parameter Code Dec Monthly Average Results No. of Samples 12 13 . . . . . . . . . . . 30 34 35 38

0 4 FINAL EFFLUENT 12 13 Parameter Unit Parameter Code Dec Monthly Average Results No. of Samples

E. Coli. G.mean /100 0 6 3 . 4 5 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 3 . 3 8 5 TSS Loading kg/d 1 0 . 1 5 5 TP Loading kg/d 0 . 3 7 5 Max pH 7 . 6 6 Min pH 7 . 0 1 . . 30 34 35 38


Email Address [email protected]/ [email protected]/[email protected]

Comments Note future Lethality analysis will be reduced to yearly analysis as premitted by ECA 6245-AB6HDR Section 8 (8)

beReturn completed form to:

1. Environmental Monitoring and Reporting Branch, MOE, at [email protected] AND 2. Your Environmental Officer at your local District/Area MOE Office. (Find your local MOE office: http://www.ene.gov.on.ca/environment) 2062 (2011/03) Page 2 of 2





Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38


0 1 5 5 4 Suspended Solids (mg/L) 0 0 0 0 6 0 1 4 2 4 TKN (mg/L) 0 0 0 2 0 2 2 4 . 4 0 4 Total Phosphorous (mg/L) 0 0 0 3 3 1 3 . 4 4

30 34 35 38


(mg/L) 0 0 0 0 1

1 4 . 8 4

Suspended Solids (mg/L) 0 0 0 0 6 1 1 8 . 3 4 Ammonia + Ammonium (mg/L) 0 0 0 1 9 2 0 . 1 4 TKN (mg/L) 0 0 0 2 0 2 . 0 Total Phosphorous (mg/L) 0 0 0 3 3 2 0 . 5 2 4



1 2 4 5 . 2











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 2 . 0 0 4 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 4 . 9 4 4 TSS Loading kg/d 1 8 . 9 8 4 TP Loading kg/d 0 . 5 4 4 Max pH 8 . 1 5 Min pH 7 . 0 5 . . 30 34 35 38










Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38



30 34 35 38


(mg/L) 0 0 0 0 1

1 4 . 5 4




1 3 2 0 . 2











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type














Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38



30 34 35 38


(mg/L) 0 0 0 0 1

1 4 . 2 4




1 3 5 8 . 8











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 2 4 . 5 4 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 3 . 8 4 4 TSS Loading kg/d 2 0 . 0 6 4 TP Loading kg/d 0 . 4 4 4 Max pH 7 . 7 8 Min pH 7 . 5 0 . . 30 34 35 38










Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38


0 6 1 5 Suspended Solids (mg/L) 0 0 0 0 6 0 7 0 5 TKN (mg/L) 0 0 0 2 0 2 1 6 . 2 4 5 Total Phosphorous (mg/L) 0 0 0 3 3 1 2 . 2 5

30 34 35 38


(mg/L) 0 0 0 0 1

1 2 . 4 5

Suspended Solids (mg/L) 0 0 0 0 6 1 1 0 . 0 5 Ammonia + Ammonium (mg/L) 0 0 0 1 9 2 0 . 1 2 5 TKN (mg/L) 0 0 0 2 0 2 . 0 Total Phosphorous (mg/L) 0 0 0 3 3 2 0 . 2 7 5



1 4 2 1 . 3











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 2 . 4 0 5 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 4 . 5 9 5 TSS Loading kg/d 1 9 . 1 1 5 TP Loading kg/d 0 . 5 1 5 Max pH 8 . 1 Min pH 7 . 4 . . 30 34 35 38










Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38



30 34 35 38


(mg/L) 0 0 0 0 1

1 2 . 5 4

Suspended Solids (mg/L) 0 0 0 0 6 1 7 . 0 4 Ammonia + Ammonium (mg/L) 0 0 0 1 9 2 0 . 1 0 4 TKN (mg/L) 0 0 0 2 0 2 . 0 Total Phosphorous (mg/L) 0 0 0 3 3 2 0 . 5 9 4



1 2 4 8 . 1











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 6 . 5 0 4 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 2 . 3 8 4 TSS Loading kg/d 7 . 3 9 4 TP Loading kg/d 0 . 6 2 4 Max pH 8 . 2 Min pH 7 . 7 . . 30 34 35 38










Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38



30 34 35 38


(mg/L) 0 0 0 0 1

1 4 . 2 4




1 1 9 8 . 5











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 2 9 . 6 4 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 3 . 2 7 4 TSS Loading kg/d 4 . 4 2 4 TP Loading kg/d 0 . 8 9 4 Max pH 7 . 8 Min pH 7 . 7 . . 30 34 35 38










Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38



30 34 35 38


(mg/L) 0 0 0 0 1

1 2 . 0 5




1 9 4 . 5











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 8 2 . 0 0 5 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 1 . 2 2 5 TSS Loading kg/d 3 . 6 7 5 TP Loading kg/d 0 . 3 3 5 Max pH 7 . 8 Min pH 6 . 4 . . 30 34 35 38










Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38


0 1 0 9 4 Suspended Solids (mg/L) 0 0 0 0 6 0 8 1 4 TKN (mg/L) 0 0 0 2 0 2 3 2 . 6 8 4 Total Phosphorous (mg/L) 0 0 0 3 3 1 2 . 9 4

30 34 35 38


(mg/L) 0 0 0 0 1

1 2 . 0 4




1 1 2 0 . 3











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 6 4 . 4 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 1 . 4 9 4 TSS Loading kg/d 5 . 9 6 4 TP Loading kg/d 0 . 1 2 4 Max pH 7 . 6 Min pH 7 . 4 . . 30 34 35 38










Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38



30 34 35 38


(mg/L) 0 0 0 0 1

1 2 . 0 5




1 1 4 0 .











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type




E. Coli. G.mean /100 0 8 0 . 4 0 5 Lethality DM % 0 . 0 Lethality Trout % 0 . 0 . CBOD Loading kg/d 1 . 6 4 5 TSS Loading kg/d 5 . 2 5 5 TP Loading kg/d 0 . 1 0 5 Max pH 8 . 9 Min pH 6 . 2 . . 30 34 35 38








2062 (2011/03) © Queen’s Printer for Ontario, 2011 Page 1 of 2


Mechanical Plants

Project Name

Colborne Wastewater Treatment Plant Mailing Address

Unit No.

Street No.

1

Street Name

Toronto Street

PO Box

357 Municipality/City/Town

Colborne

Province

ON

Postal Code

K0K 1S0 Operating Authority

The Corporation of the Township of Cramahe Mailing Address

Unit No.

Street No.

Street Name

Same As Above

PO Box


Province

Postal Code

File No.


Days

Discharge Type

Update Code Month Year

4 6 1 2 0 0 0 0 0 8 8 1 1 19 3 0 2 R

1 2 3 11 16 19 20 21 22 80


12 13 Total Flow (103m

3 ) 5 0 0 1 0 3 3 0 . 1 6 3

Average Daily Flow (103m

3/d) 5 0 0 1 5 3 1 . 0 0 5

Maximum Daily Flow (103m

3/d) 5 0 0 2 0 3 1 . 9 3 6

30 34 35 38 46

2 6 BYPASS No. of Occurrences

12 13 Plant Bypass Volume (103m

3) 5 0 0 2 6

3 .

Duration (hrs) 8 0 5 6 3 1 . Secondary Bypass Volume (10

3m

3) 5 0 0 4 0 3 .

Duration (hrs) 8 0 5 6 5 1 . 30 34 35 38

0 3 RAW SEWAGE No. of Samples

12 13 BOD5 (mg/L) 0 0 0 0 1

0 1 1 5 4

Suspended Solids (mg/L) 0 0 0 0 6 0 1 1 4 4

TKN (mg/L) 0 0 0 2 0 2 3 0 . 5 5 4

Total Phosphorous (mg/L) 0 0 0 3 3 1 3 . 1 4 30 34 35 38


(mg/L) 0 0 0 0 1

1

1 . 7

4




1 1 7 1 . 6 Chlorine Dosage (mg/L as Cl2) 8 0 4 1 0 1 5 . 6 Chlorine Residual (mg/L as Cl2) 8 0 4 2 0 1 0 . 0 1 0 5


Operator Telephone Number

905-355-2982

Email Address

[email protected] / [email protected]/[email protected]

Comments


1. Environmental Monitoring and Reporting Branch, MOE, at [email protected] AND

2. Your Environmental Officer at your local District/Area MOE Office. (Find your local MOE office: http://www.ene.gov.on.ca/environment)



2062 (2011/03) Page 2 of 2


Mechanical Plants

Project Name

Colborne Wastewater Treatment Plant Mailing Address

Unit No.

Street No.

1

Street Name

Toronto Street

PO Box

357 Municipality/City/Town

Colborne

Province

ON

Postal Code

K0K 1S0 Operating Authority

The Corporation of The Township of Cramahe Mailing Address

Unit No.

Street No.

Street Name

Same as above

PO Box


Province

Postal Code

File No.


Days

Discharge Type

Update Code Month Year

4 6 1 2 0 0 0 0 0 8 8 1 1 19 3 0 2 R

1 2 3 11 16 19 20 21 22 80

C.P. RAW SEWAGE

3 6 Parameter Unit Parameter Code Dec Monthly Average Results No. of Samples

12 13 .

.

.

.

.

.

.

.

.

.

. 30 34 35 38

0 4 FINAL EFFLUENT

12 13 Parameter Unit Parameter Code Dec Monthly Average Results No. of Samples

E. Coli. G.mean /100 0 1 0 . 5 0 4

Lethality DM % 0 . 0

Lethality Trout % 0 . 0

.

CBOD Loading kg/d 1 . 7 6 4

TSS Loading kg/d 5 . 0 3 4

TP Loading kg/d 0 . 0 7 4

Max pH 7 . 6 4 5

Min pH 7 . 3 8 5

.

. 30 34 35 38

Operator Telephone Number

905-355-2982

Email Address

[email protected]/ [email protected]/[email protected] Comments

Note future Lethality analysis will be reduced to yearly analysis as premitted by ECA 6245-AB6HDR Section 8 (8)


1. Environmental Monitoring and Reporting Branch, MOE, at [email protected] AND

2. Your Environmental Officer at your local District/Area MOE Office. (Find your local MOE office: http://www.ene.gov.on.ca/environment)





Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type






30 34 35 38



30 34 35 38


(mg/L) 0 0 0 0 1

1 2 . 7 4

Suspended Solids (mg/L) 0 0 0 0 6 1 8 . 7 4 Ammonia + Ammonium (mg/L) 0 0 0 1 9 2 0 . 0 1 4 TKN (mg/L) 0 0 0 2 0 2 . 0 Total Phosphorous (mg/L) 0 0 0 3 3 2 0 . 1 4



1 1 7 0 . 0











Street No. 1


PO Box 357


Province ON

Postal Code K0K 1S0


Street No.


PO Box


Province

Postal Code

File No.


Days

Discharge Type













Appendix E – Lethality Testing

Page 21


Appendix F - Calibration Reports

Page 22

FIELD SERVICES REPORT REPORT OF: Mike Humphries DATE OF SERVICE: August 01, 2019 CUSTOMER / ADDRESS:

Colborne WWTP Ontario Street

Colborne, Ontario CONTACT: Ted Joynt EMAIL: PURPOSE FOR SERVICE: Check operation and calibration of OCM III on Raw Influent coming into Plant. SYSTEM CONFIGURATION: OCM III, REV 3.31 XRS-5C transducer TS2 temperature sensor APPLICATION: Primary element: 6” Parshall Flume Maximum flow: 6000 m³/day Maximum head: 34.0746 cm OBSERVATIONS / CHANGES MADE: Totalizer As Found 1721799 m³ Totalizer As Left 1721818 m³ Zero As Found 67.390500 cm Zero As Left 66.731420 cm Change in Zero 0.659080 m

OCM Flow Table Head

Applied (m)

Head Displayed

(m)

Error (%)

Calculated Flow (m³/d)

Flow Displayed (m³/d)

Error (%)

Calculated MA

Output

Measured mA Output

Error (%)

0.00 0.0000 0.00 0.00 0.00 0.00 4.00 4.00 0.00

0.10 0.0998 ‐0.20 865 863 ‐0.21 6.31 6.30 ‐0.10

0.20 0.2003 0.15 2585 2595 0.37 10.89 10.91 0.14

0.30 0.2995 ‐0.17 4906 4899 ‐0.15 17.08 17.05 ‐0.20

0.34 0.3396 ‐0.34 6000 5985 ‐0.25 20.00 19.92 ‐0.40

CONCLUSIONS / RECOMMENDATIONS: OCM III is functioning as expected giving good accurate results.

OPEN CHANNEL METER III USER: Colborne WWTP SERIAL #: LOCATION: Inlet TAG #: Raw

Par As found

As Left

Description Par As found

As left

Description

0 0 Language U0 1.58 1 0 Dimensional units U1 2 0 Temperature units U2 3 0 Primary element U3 4 1 Calculation method U4 5 7 Units flow rate F 4 X OK Time 6 6000 Flow at max head F 5 X OK Date 7 34.0746 Height of max head F 6 3.32 Eprom # 8 0 Volts in at zero velocity F 11 Totalizer master reset9 0 Velocity @ 5 volts in D0 15.78 Head 10 Velocity @ max flow D1 1766 Flow rate 11 N/a D2 844499.2 Short totalizer * 12 N/a D3 5856 C Flow rate maximum13 Display damping D4 0 C Flow rate minimum14 Display lighting D5 24.64 Temperature 15 1 Relay 1 assignment D6 37.46 C Temperature max.16 Relay 1 high setpoint D7 -22.16 C Temperature min.17 Relay 1 low setpoint D8 Velocity 18 Relay 2 assignment D9 52 Target range 19 Relay 2 high setpoint D10 8.83 mA output 20 Relay 2 low setpoint D11 DC volts internal21 Relay 3 assignment D12 Velocity volts 22 Relay 3 high setpoint D13 Auxiliary input volts23 Relay 3 low setpoint D14 9052 Temperature sensor ohms24 mA assignment D15 Self test checksum25 Custom mA D16 7 C Restarts 26 Span mA D17 0 3 Exceptions 27 30 Damping mA (sec) D18 59 Echos 28 Emulator tracking mA o/p A0 Head point 1 29 60 Fail-safe timer (sec) A1 Flow point 1 30 Fail-safe analog mode A2 Head point 2 31 Failsafe mA (default) A3 Flow point 2 32 3 Totalizer multiplier A4 Head point 3 33 2 Display flow-rate dec point # A5 Flow point 3 34 Printer mode A6 Head point 4 35 Printer timing A7 Flow point 4 36 Measurement interval A8 Head point 5 37 5 Serial data rate (baud) A9 Flow point 5 38 Site # A10 Head point 6 39 2 Data logging rate A11 Flow point 6 40 Log rapid setpoint A12 Head point 7 41 Log normal set point A13 Flow point 7 42 Head determination A14 Head point 8 43 Volts in for zero head A15 Flow point 8 44 Head @ 5 volts in A16 Head point 9 45 0.5 Low cutoff head A17 Flow point 9 46 67.3905 66.73142 Range @ zero head A18 Head point 1047 30.48264 Blanking distance A19 Flow point 10 A20 Head point 11 A21 Flow point 11

FIELD SERVICES REPORT REPORT OF: Mike Humphries DATE OF SERVICE: August 01, 2019 CUSTOMER / ADDRESS:

Colborne WWTP Ontario Street

Colborne, Ontario CONTACT: Ted Joynt EMAIL: PURPOSE FOR SERVICE: Check operation and calibration of OCM III measuring Final Effluent leaving the plant. SYSTEM CONFIGURATION: OCM III, REV 3.31 XRS-5C transducer TS2 temperature sensor APPLICATION: Primary element: 6” Parshall Flume Maximum flow: 6000 m³/day Maximum head: 34.0746 cm OBSERVATIONS / CHANGES MADE: Totalizer As Found 4572569 m³ Totalizer As Left 4572583 m³ Zero As Found 89.599990 cm Zero As Left 88.382110 cm Change in Zero 1.217880 m

OCM Flow Table Head

Applied (m)

Head Displayed

(m)

Error (%)

Calculated Flow (m³/d)

Flow Displayed (m³/d)

Error (%)

Calculated MA

Output

Measured mA Output

Error (%)

0.00 0.0000 0.00 0.00 0.00 0.00 4.00 3.98 ‐0.50

0.10 0.1001 0.10 865 868 0.37 6.31 6.30 ‐0.10

0.20 0.2002 0.10 2585 2583 ‐0.10 10.89 10.88 ‐0.13

0.30 0.3010 0.33 4906 4924 0.36 17.08 17.14 0.33

0.34 0.3410 0.07 6000 6012 0.20 20.00 20.02 0.10

CONCLUSIONS / RECOMMENDATIONS: OCM III is functioning as expected giving good accurate results.

OPEN CHANNEL METER III USER: Colborne WWTP SERIAL #: LOCATION: Effluent TAG #: Final

Par As found

As Left

Description Par As found

As left

Description

0 0 Language U0 1.58 1 0 Dimensional units U1 2 0 Temperature units U2 3 0 Primary element U3 4 1 Calculation method U4 5 7 Units flow rate F 4 X OK Time 6 6000 Flow at max head F 5 OK Date 7 34.0746 Height of max head F 6 3.31 Eprom # 8 0 Volts in at zero velocity F 11 Totalizer master reset9 0 Velocity @ 5 volts in D0 4.86 Head 10 Velocity @ max flow D1 275 Flow rate 11 N/a D2 458812.6 Short totalizer * 12 N/a D3 6511 C Flow rate maximum13 Display damping D4 0 C Flow rate minimum14 Display lighting D5 26.84 Temperature 15 1 Relay 1 assignment D6 34.00 C Temperature max.16 Relay 1 high setpoint D7 -22.16 C Temperature min.17 Relay 1 low setpoint D8 Velocity 18 Relay 2 assignment D9 85 Target range 19 Relay 2 high setpoint D10 4.67 mA output 20 Relay 2 low setpoint D11 DC volts internal21 Relay 3 assignment D12 Velocity volts 22 Relay 3 high setpoint D13 Auxiliary input volts23 Relay 3 low setpoint D14 8763 Temperature sensor ohms24 mA assignment D15 Self test checksum25 Custom mA D16 7 C Restarts 26 Span mA D17 0 3 Exceptions 27 30 Damping mA (sec) D18 100 Echos 28 Emulator tracking mA o/p A0 Head point 1 29 60 Fail-safe timer (sec) A1 Flow point 1 30 Fail-safe analog mode A2 Head point 2 31 Failsafe mA (default) A3 Flow point 2 32 3 Totalizer multiplier A4 Head point 3 33 2 Display flow-rate dec point # A5 Flow point 3 34 Printer mode A6 Head point 4 35 Printer timing A7 Flow point 4 36 Measurement interval A8 Head point 5 37 5 Serial data rate (baud) A9 Flow point 5 38 Site # A10 Head point 6 39 2 Data logging rate A11 Flow point 6 40 Log rapid setpoint A12 Head point 7 41 Log normal set point A13 Flow point 7 42 Head determination A14 Head point 8 43 Volts in for zero head A15 Flow point 8 44 Head @ 5 volts in A16 Head point 9 45 0.5 Low cutoff head A17 Flow point 9 46 89.59999 88.38211 Range @ zero head A18 Head point 1047 50 Blanking distance A19 Flow point 10 A20 Head point 11 A21 Flow point 11

DTM Version: 3.17.00 Page 1/3

Flowmeter Verification Certificate Transmitter

Colborne

Customer

Order code

PROMAG 53 P DN350

Device type

EA095116000

Serial number

V2.03.00

Software Version Transmitter

08/01/2019

Verification date

WW header to Lake

Plant

--------

Tag Name

0.9786 - 0.9786

K-Factor

-13

Zero point

V1.05.03

Software Version I/O-Module

11:48

Verification time

Verification result Transmitter: Passed

Test item Result Applied Limits

Amplifier Passed Basis: 0.55 %

Current Output 1 Passed 0.05 mA

Pulse Output 1 Not tested 0 P

Test Sensor Passed

FieldCheck Details

550149Production number

1.07.08Software Version

03/2019Last Calibration Date

Simubox Details

8781637Production number

1.00.01Software Version

03/2019Last Calibration Date

Date Operator's Sign Inspector's Sign

Overall results: The achieved test results show that the instrumment is completely functional, and the measuring results lie within +/- 1% of the original calibration. 1)

The calibration of the Fieldcheck test system is fully traceable to national standards.

1) Prerequisite is an additional proof of electrode integrity with a high voltage test.

/3

FieldCheck - Result Tab TransmitterCustomer Colborne

Order code

Device type PROMAG 53 P DN350

Serial number EA095116000

Software Version Transmitter V2.03.00

Verification date 08/01/2019

Plant WW header to Lake

Tag Name --------

K-Factor 0.9786 - 0.9786

Zero point -13

Software Version I/O-Module V1.05.03

Verification time 11:48

Verification Flow end value ( 100 % ): 384.845 l/s

Flow speed 4.00 m/s

Passed / Failed Test item Simul. Signal Limit Value Deviation

Test Transmitter

Amplifier 19.242 l/s (5%) 1.50 % -0.17 %

38.485 l/s (10.0%) 1.00 % 0.04 %

192.424 l/s (50.0%) 0.60 % 0.00 %

384.846 l/s (100%) 0.55 % 0.05 %

Current Output 1 4.000 mA (0%) 0.05 mA 0.004 mA

4.800 mA (5%) 0.05 mA 0.003 mA

5.600 mA (10.0%) 0.05 mA -0.008 mA

12.000 mA (50.0%) 0.05 mA 0.004 mA

20.000 mA (100%) 0.05 mA 0.009 mA

Pulse Output 1 --- --- ---

Start value Limits range Measured value

Test Sensor

Coil Curr. Rise 29.600 ms0.000..52.500

ms30.393 ms

Coil Curr. Stability --- ---

Electrode Integrity mV 0.0..300.001 mV 16.243 mV

Legend of symbols

Passed Failed not tested not testable Attention

/3

FieldCheck: Parameters TransmitterCustomer Colborne

Order code

Device type PROMAG 53 P DN350

Serial number EA095116000

Software Version Transmitter V2.03.00

Verification date 08/01/2019

Plant WW header to Lake

Tag Name --------

K-Factor 0.9786 - 0.9786

Zero point -13

Software Version I/O-Module V1.05.03

Verification time 11:48

Curent Output Assign Current Range Value 0_4mA Value 20 mA

Terminal 26/27VOLUME

FLOW4-20 mA active 0.0 l/s 250.01 l/s

Pulse Output Assign Pulse Value Output signal Pulse width

Terminal 24/25VOLUME

FLOW0.114 m3/P

Passive/Positive

100.01 ms

Actual System Ident. 123.0


Appendix G- Bypass Report

Page 23

Colborne WWTP Quarterly Bypass and Plant Overflow Report 2019

Plant Works # 120000088

Quarter Event # Date Volume Duration Reason/Cause Treatment Disinfectionm3 hr

Feb-14 N/A N/A N/A N/A No bypass events N/A N/AMay-15 N/A N/A N/A N/A No bypass events N/A N/AAug-14 N/A N/A N/A N/A No bypass events N/A N/ANov-15 N/A N/A N/A N/A No bypass events N/A N/A

The plant has a peak flow anttenuation pond to which some flow is diverted during high flows and directed back for treatment as inflow diminishes.

This report is submitted to fufill requirements of ECA 6245-AB6HDR Section 4 (3)

Corporation of the Township of Cramahe Village of Colborne Wastewater Treatment Plant Performance Repor t 2019

Appendix H- Operators Licensing

Page 24

2019 annual summary report amended environmental ...€¦ · 1. a summary and interpretation of all...

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