PERRL Emission Reduction Claim Report 2003 and City of London W12A Landfill Gas Capture and Combustion Project

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1 PERRL Emission Reduction Claim Report 2003 and 2004 City of London W12A Landfill Gas Capture and Combustion Project

2 TABLE OF CONTENTS SECTION A SUMMARY OF LANDFILL GAS FLARING IN 2003 AND 2004 SECTION B ER CLAIM FORMS SECTION C UPDATED TEMPLATES AND ATTACHMENTS REPORT SECTION D DAILY SUMMARY OF FLARE OPERATING CONDITIONS SECTION E AUDITOR S REPORT PERRL Emission Reduction Claim Report 2003 and 2004

3 SECTION A SUMMARY OF LANDFILL GAS FLARING IN 2003 AND 2004 Summary of W12A Landfill Gas Flaring 2003 On June 23, 2003, a temporary landfill gas (LFG) flaring system became operational at the City of London s W12A landfill. However, the data logger was not operational until September 19, Therefore, the LFG quantities flared between June 23 and September 19 are not included in the determination of emission reduction credits (ERCs). The temporary LFG flare system remained operational until December 19, During that time, tonnes of methane were destroyed in the flare. Based on methane s global warming potential (GWP = 21), this is equivalent to 5,660 tonnes of greenhouse gases avoided (GHGs expressed in terms of equivalent carbon dioxide). Summary of W12A Landfill Gas Flaring 2004 On June 20, 2004, the permanent LFG flaring system became operational at the W12A landfill. Initially, the system was collecting around 0.35 standard cubic metres per second (or 750 Scfm) of LFG with a methane content of 45%. This is equivalent to approximately 4,100 tonnes of methane destroyed (85,000 tonnes of greenhouse gases) per year had this LFG flowrate been maintained with minimal down time. However, by early December, LFG gas flow to the LFG flare had dropped to around 0.24 m 3 /s (500 Scfm) with a methane content of 50%. This is equivalent to approximately 2,200 tonnes of methane destroyed (46,000 tonnes of greenhouse gases) per year. Some of this drop can be attributed to depletion of pent-up landfill gas. However, most of this drop can be attributed to the commissioning and operational problems outlined below. During 2004, 852 tonnes of methane were destroyed in the flare. This is equivalent to 17,897 tonnes of greenhouse gases avoided. The quantity of GHG emission reductions created by the landfill flare in 2004 was approximately 25% of the amount of gas stated in the Purchase and Sale of Greenhouse Gas Emission Reduction Agreement between the City of London and Environment Canada. The reduced quantity is the result of three factors: 1. Delays in Flare Delivery - Delays in the fabrication of the flare by LFG Specialties in Ohio delayed start up of the system until the end of June. As a result the system was only operational for approximately 6 months in In future years, GHG emission reductions should double with year round operation. 2. Commissioning/Operational Problems - Since beginning operation, the flare has been shut down approximately 20% of the time due to commissioning/operational problems. Commissioning problems have included valves sticking in cold weather (valves have since been insulated) and fluctuating pressures in collection line. The latter problem periodically caused the system to shut down because of high suction pressures at the flare. It was only after several shutdowns that the cause of the problem was determined (pressure testing plug left in collection line). The pressure PERRL Emission Reduction Claim Report 2003 and 2004

4 testing plug was removed in late December Subsequently, methane content at the flare increased from 50% to 70%. An ongoing operational problem that is continuing to cause the flare to periodically shut down is the poor electrical supply to the landfill. Short term power fluctuations (i.e., equivalent to lights flickering) can cause the flare to shut down. The City plans on installing an uninterrupted power supply (UPS) at the flare in Base Flow to the Flare was Less Than Originally Estimated - There is less gas being collected when the system is running than originally projected. The main reason for the reduced flow is because no gas is being collected from an area that was expected to produce significant gas quantities given the type and age of the waste buried. A test well drilled in this area produced high gas flows (0.03 m 3 /s or 60 cfm) however the nine production wells drilled in this area are flooded. Calculation Method for Methane Destruction The W12A Landfill s LFG flaring system is equipped with on-line continuous monitors for the following: Oxygen concentration (percent by volume) Methane concentration (percent by volume) Flare temperature ( C) LFG flow to the flare (cubic feet per minute, corrected to standard conditions) The LFG flaring system s datalogger records these data every two minutes. The quantities of methane destroyed in the flare were calculated in two-minute intervals based on the following formula: M CH4 = DRE V LFG c CH4 ρ CH4 Where, M CH4 = mass flowrate of methane to LFG flare (kilograms/minute) DRE = destruction removal efficiency (99%) V LFG = volume flowrate of LFG to flare (standard cubic feet per minute) c CH4 = methane concentration (percent by volume) ρ CH4 = methane density at standard conditions ( lbs/sft 3 ) Data from periods where the LFG flare system was not in operation (i.e., when the LFG gas flowrate fell below 300 Scfm) were excluded in these calculations. Example Calculation On July 2, 2004 at 3:30 pm, the following operating conditions were observed: Methane concentration % LFG flow to the flare 794 cfm (or Sft 3 /minute) PERRL Emission Reduction Claim Report 2003 and 2004

5 Based on the formula above: M CH4 = DRE V LFG c CH4 ρ CH4 = kg/lbs Sft 3 /minute lbs/ Sft 3 = 7.66 kg/minute W12A Landfill Gas Flaring System - Plans for 2005 As of December 31, 2004, the LFG flaring system was running at around 70% methane concentration with a LFG flowrate around 0.21 m 3 /s (450 Scfm). This is equivalent to approximately 3,100 tonnes of methane destroyed (65,000 tonnes of greenhouse gases) per year if this LFG flowrate is maintained with minimal down time. The City has approved a capital expenditure of $600,000 in 2005 in order to increase the base flow of landfill gas. Options for increasing the flow are: Decrease Well Spacing in Existing Well Field - The existing gas wells that are spaced relatively far apart and the zone of influence for the wells do not overlap. Consideration will be given to adding additional wells in the existing well fields. Lower Leachate Levels in Flooded Wells - Alternatives for lowering the leachate levels in the flooded wells will be examined. Drilling additional wells beside the gas production wells and pumping the leachate is likely to be the most cost effective method. A test well will likely be drilled in early 2005 to determine the effectiveness of this alternative. Expanding Into New Areas - Approximately 8 hectares of landfill reached capacity and was capped in Consideration will be given to expanding the well field into this area. It is anticipated that the work mentioned above could increase the LFG flowrate up to 0.57 m 3 /s (1200 Scfm) with a methane concentration of 50%. This could increase the annual methane destruction rate up to approximately 5,700 tonnes of methane (120,000 tonnes of greenhouse gases) y:\shared\solwaste\w12a\landfill gas\perrl submission\summary of w12a landfill gas flaring doc PERRL Emission Reduction Claim Report 2003 and 2004

6 SECTION B ER CLAIM FORMS PERRL Emission Reduction Claim Report 2003 and 2004

7 ER CLAIM FORM SELLER Information Company Name Contact Name Contact Title City of London Mr. Peter Steblin, P.Eng. General Manager of Environmental Services & City Engineer Street 300 Dufferin Ave., P.O. Box 5035 City London Province Postal Code Phone Ontario N6A 4L x4936 Fax Project Results Project Name ER Vintage (Calendar Year ERs created) psteblin@london.ca ER Start Date September 18, 2003 ER End Date December 19, 2003 ER Quantity (Tonnes CO 2 e) 5,660 Price per Tonne ($) 2.96 ER Claim Value $16, Surplus Criteria Relevant Jurisdictional Regulations Operating Standards Voluntary Agreements Other Emission Reduction Agreements Signed Landfill Gas Capture and Combustion Project at the W-12A Landfill Temporary Flare 2003 None no changes to regulations nor landfill operations that would make landfill gas collection mandatory for W12A Landfill None None None Project Costs Capital Cost to date $ - O&M Cost to date $ 33,372 Ownership and Partnerships Project and ER Ownership (leave blank if unchanged) Project Partnerships (leave blank if unchanged) Project Funding New Funding Sources (leave blank if unchanged) Federal Funding Received (leave blank if unchanged) Report Sign-off As a duty authorized officer of the proponent entity, I submit this report to be true and accurate: Signature of Officer Date

8 ER CLAIM FORM SELLER Information Company Name Contact Name Contact Title City of London Mr. Peter Steblin, P.Eng. General Manager of Environmental Services & City Engineer Street 300 Dufferin Ave., P.O. Box 5035 City London Province Postal Code Phone Ontario N6A 4L x4936 Fax Project Results Project Name ER Vintage (Calendar Year ERs created) psteblin@london.ca ER Start Date June 20, 2004 ER End Date December 31, 2004 ER Quantity (Tonnes CO 2 e) 17,897 Price per Tonne ($) 2.96 ER Claim Value $52, Surplus Criteria Relevant Jurisdictional Regulations Operating Standards Voluntary Agreements Other Emission Reduction Agreements Signed Project Costs Landfill Gas Capture and Combustion Project at the W-12A Landfill Permanent Flare 2004 None no changes to regulations nor landfill operations that would make landfill gas collection mandatory for W12A Landfill None None None Capital Cost to date $ 971,431 O&M Cost to date $ 62,785 Ownership and Partnerships Project and ER Ownership (leave blank if unchanged) Project Partnerships (leave blank if unchanged) Project Funding New Funding Sources (leave blank if unchanged) Federal Funding Received (leave blank if unchanged) Report Sign-off As a duty authorized officer of the proponent entity, I submit this report to be true and accurate: Signature of Officer Date

9 SECTION C UPDATED TEMPLATES AND ATTACHMENTS REPORT PERRL Emission Reduction Claim Report 2003 and 2004

10 Table: Project Data Template General Element Information 1 Element Identifier PE1 PE2 2 Element Name PE1 - Methane from landfill PE2 - Methane captured without a gas capture and combusted system 3 Element Main Activity Type Operation Operation 4 Element Description Current emissions (m 3 /day) from W12A Landfill with no gas capture system in place Methane (m 3 /day) captured and combusted by gas capture and combustion system 5 Type of Element (main or ancillary) Main Main 6 Type of Element (direct or indirect) Direct Direct 7 Element Reference Unit kgs of methane emitted kgs of methane destroyed 8 Expected Life of Element (years) > 50 years at least 20 years 9 Type of Element Emission Estimation Method US EPA LandGEM model Flow measurement and calculation Element Input Information 10 Name of Input Waste Landfill gas 11 Type of Input (energy, mass, GHG) Mass Volume of gas 12 Number of Units of Input Units of Measure tonnes/day Scfm (average) 14 GHG/Unit of Input NA NA 15 Units of Measure NA NA 16 Name of Input NA Methane concentration 17 Type of Input (energy, mass, GHG) Concentration 18 Number of Units of Input Units of Measure % by volume 20 GHG/Unit of Input NA 21 Units of Measure 22 Name of Input NA Methane density 23 Type of Input (energy, mass, GHG) Mass density 24 Number of Units of Input Units of Measure lbs/scf 26 GHG/Unit of Input 27 Units of Measure

11 Element Output Information 28 Name of Output Methane emitted to Methane destroyed atmosphere 29 Type of Output (energy, mass, GHG) mass mass 30 Number of Units of Output 20,000 6, Units of Measure kgs of CH 4 per day kg of CH 4 per day 32 GHG/Unit of Output 421, , Units of Measure kgs of CO 2 e per day kg of CO 2 e per day 34 Name of Output NA NA 35 Type of Output (energy, mass, GHG) 36 Number of Units of Output 37 Units of Measure 38 GHG/Unit of Output 39 Units of Measure 40 Name of Output NA NA 41 Type of Output (energy, mass, GHG) 42 Number of Units of Output 43 Units of Measure 44 GHG/Unit of Output 45 Units of Measure Element GHG Overview Information 46 Element GHG Intensity (CO 2 e/unit) Units of Measure (common for all kg CO 2 e / tonne waste kg CO 2 e / m 3 LFG elements) 48 Element Installation GHG Emissions Immaterial Immaterial 49 Units of Measure NA NA 50 Element Maintenance GHG Emissions Immaterial Immaterial 51 Units of Measure NA NA 52 Element Decommissioning GHG Immaterial Immaterial Emissions 53 Units of Measure NA NA Environmental Information 54 Comments about Air Other volatile organic compounds are emitted from landfills, some of them toxic 55 Comments about Water Landfill leachate collection and mitigation is part of the landfill design 56 Comments about Land Use of existing land adjacent to the landfill minimises the impacts on other land areas Volatile organic compounds are also destroyed in the landfill gas combustor The gas collection system will have no effect on the leachate collection and mitigation system The gas collection system will have no effect on land outside the landfill 57 Comments about Wildlife The landfill has measures The gas collection system in place to minimize impacts will have no effect on on wildlife wildlife or the landfill s wildlife protection measures

12 Table: Benchmark Data Template General Element Information 1 Element Identifier BE1 NA 2 Element Name BE1 - Methane emitted from landfill without gas capture system 3 Element Main Activity Type Landfilling municipal solid waste 4 Element Description Current emissions from W12A Landfill with no gas capture system in place 5 Type of Element (main or ancillary) Main 6 Type of Element (direct or indirect) Direct 7 Element Reference Unit kgs of methane emitted 8 Expected Life of Element (years) > 50 years 9 Type of Element Emission Estimation Method LandGEM model Element Input Information 10 Name of Input Waste 11 Type of Input (energy, mass, GHG) Mass 12 Number of Units of Input Units of Measure tonnes / day 14 GHG/Unit of Input NA 15 Units of Measure NA 16 Name of Input NA 17 Type of Input (energy, mass, GHG) 18 Number of Units of Input 19 Units of Measure 20 GHG/Unit of Input 21 Units of Measure 22 Name of Input NA 23 Type of Input (energy, mass, GHG) 24 Number of Units of Input 25 Units of Measure 26 GHG/Unit of Input 27 Units of Measure Element Output Information 28 Name of Output Methane emitted to atmosphere 29 Type of Output (energy, mass, GHG) Mass 30 Number of Units of Output 20, Units of Measure kgs of CH4 per day 32 GHG/Unit of Output 421, Units of Measure kgs of CO 2 e per day 34 Name of Output NA 35 Type of Output (energy, mass, GHG) 36 Number of Units of Output 37 Units of Measure 38 GHG/Unit of Output 39 Units of Measure 40 Name of Output NA 41 Type of Output (energy, mass, GHG) 42 Number of Units of Output 43 Units of Measure

13 44 GHG/Unit of Output 45 Units of Measure Element GHG Overview Information 46 Element GHG Intensity (CO 2 e/unit) Units of Measure (common for all kg CO 2 e / tonne waste elements) 48 Element Installation GHG Emissions Immaterial 49 Units of Measure NA 50 Element Maintenance GHG Emissions Immaterial 51 Units of Measure NA 52 Element Decommissioning GHG Immaterial Emissions 53 Units of Measure NA Environmental Information 54 Comments about Air Other volatile organic compounds are emitted from landfills, some of them toxic 55 Comments about Water Landfill leachate collection and mitigation is part of the landfill design 56 Comments about Land Use of existing land adjacent to the landfill minimises the impacts on other land areas 57 Comments about Wildlife The landfill has measures in place to minimize impacts on wildlife

14 Table: Delta Report Template PERRL Emission Reduction Calculation 1 Total Benchmark GHG Emissions per year (Tonnes CO 2 e) Direct Indirect Total , , , , , , , , , , , ,000 8 Total 1,704,000 1,704,000 9 Total Project GHG Emissions per year (Tonnes CO 2 e) Direct Indirect Total , , , , ,557 74, ,000 45, ,000 49, , , Total 754, , Total GHG Emission Reductions/Removals per year (Tonnes CO 2 e) Direct Indirect Total ,660 5, ,897 17, ,443 86, , , , , , , Total 950, , GHG Emission Reductions/Removals Offered for Sale (Tonnes CO 2 e) , , , , , Total 350,000

15 SECTION D DAILY SUMMARY OF FLARE OPERATING CONDITIONS PERRL Emission Reduction Claim Report 2003 and 2004

16 Average Daily Methane Capture with Temporary Flare

17 LFG Flow (cfm) CH4 Conc. (%v) CH4 kg Day Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Sep-03 Total Sep-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total

18 LFG Flow (cfm) CH4 Conc. (%v) CH4 kg Day Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Oct-03 Total Oct-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average

19 LFG Flow (cfm) CH4 Conc. (%v) CH4 kg Day 0 14-Nov-03 Total Nov-03 Average 2 15-Nov-03 Total Nov-03 Average 1 16-Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average 2 23-Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Nov-03 Total Nov-03 Average Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average 0 6-Dec-03 Total Dec-03 Average 0 7-Dec-03 Total Dec-03 Average 0 8-Dec-03 Total Dec-03 Average 0 9-Dec-03 Total

20 LFG Flow (cfm) CH4 Conc. (%v) CH4 kg Day Dec-03 Average 0 10-Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average 0 12-Dec-03 Total Dec-03 Average 0 13-Dec-03 Total Dec-03 Average 0 14-Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average Dec-03 Total Dec-03 Average 0 19-Dec-03 Total Dec-03 Average

21 LFG Collection Data from Temporary Flare System (2003) Date & Time LFG Flow (cfm) CH4 Conc. (%v) O2 Conc. (%v) Gas Temperature ( C) CH4 cfm CH4 m3/h CH4 kg/h CH4 kg Month Day 97 September Average 24-Sep September Total ######### October Average 12-Oct October Total ######### November Average 16-Nov November Total ######### 47 December Average 10-Dec December Total ######### 115 Grand Average 10-Oct Grand Total ######### For Unrecorded Period (June 23 - Sept. 18) 172 kg/h Average Collection Rate (Oct. - Nov.) 87 days without datalogger kg estimated methane captured For Recorded Period (Sept Dec. 19) kg methane captured Estimated Total for kg methane captured 99.00% Methane Destruction Efficiency 21 Methane GWP tonnes CO2e destroyed

22 From To Methane Flared (tonnes) Equivalent CO2e (tonnes) 20-Jun Jun Jun Jun June 2004 Total

23 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH4 tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total - - Grand Average Grand Total

24 Emission Reduction Emission Reduction Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) tonne/yr CH 4 tonne/yr CO 2eq tonnes CH4 tonnes CO2eq Average Total Average Total Average Total Average Total Grand Average Grand Total

25 Methane Flared (tonnes) Equivalent CO2e (tonnes) Equivalent CO2e (Mg/day)) From To 01-Jul Jul Jul Jul Jul Jul Jul Jul Jul Jul , July 2004 Total 194 4,

26 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH4 tonnes CO2eq Average Total Average Total Average Total Grand Average Grand Total

27 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Grand Average Grand Total

28 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

29 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Average Grand Total

30 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Average Grand Total ,219.96

31 Methane Flared (tonnes) Equivalent CO2e (tonnes) From To 01-Aug Aug Aug Aug Aug Aug Aug Aug Aug Aug August 2004 Total 135 2,826

32 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH 4 tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

33 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Grand Total Grand Average

34 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Grand Average Grand Total

35 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Average Grand Total

36 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total /30/2004 Average /30/2004 Total /31/2004 Average /31/2004 Total Grand Average Grand Total

37 From Methane Flared (tonnes) Equivalent CO2e (tonnes) To 01-Sep Sep Sep Sep Sep Sep Sep Sep Sep Sep September 2004 Total 139 2,916

38 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Grand Total Grand Average

39 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr C tonne/yr COtonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average 2 (1) Total Average Total Average Total Grand Total Grand Average

40 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total /9/2004 Average /9/2004 Total /19/2004 Average /19/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total Grand Total Grand Average

41 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq 19/9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total Grand Total Grand Average

42 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq 26/9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total /9/2004 Average /9/2004 Total Grand Total Grand Average

43 Methane Flared (tonnes) Equivalent CO2e (tonnes) From To 01-Oct Oct Oct Oct Oct Oct Oct Oct Oct Oct Oct Oct October 2004 Total 108 2,264

44 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr Ctonnes CH tonnes CO2eq Average Total Average Total Grand Total Grand Average

45 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr C tonne/yr C tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

46 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr C tonne/yr C tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

47 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr C tonne/yr C tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

48 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total - - Grand Total Grand Average

49 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2eq tonnes CH tonnes CO2eq Average Total - - Grand Total 0 - Grand Average 1 12

50 From Methane Flared (tonnes) Equivalent CO2e (tonnes) To 01-Nov Nov Nov Nov Nov Nov Nov Nov Nov Nov November 2004 Total 92 1,930

51 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total - - Grand Total Grand Average

52 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

53 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total - - Grand Total Grand Average 1 12

54 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average (5) (116) Total Average Total Average Total Average Total Grand Total Grand Average

55 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Average Total Average Total Average Total Grand Total Grand Average tonne/yr CH 4 tonne/yr CO 2eq

56 Methane Flared (tonnes) Equivalent CO2e (tonnes) From To 01-Dec Dec Dec Dec Dec Dec Dec Dec Dec Dec December 2004 Total 125 2,620

57 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Grand Total Grand Average

58 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

59 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average

60 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Average Total - - Grand Total Grand Average

61 Time Date O 2 (% by volume) CH 4 (% by volume) Temperature (C) Flow Rate (scfm) Emission Reduction Emission Reduction tonne/yr CH 4 tonne/yr CO 2e tonnes CH tonnes CO2eq Average Total Average Total Average Total Average Total Average Total Average Total Grand Total Grand Average 7 47

62 SECTION E AUDITOR S REPORT PERRL Emission Reduction Claim Report 2003 and 2004

63 D. H. Lyons D. H, Lyons Phone (416) Keele Street FAX (416) Toronto, ON M6P 2K1 Mobile (416) Greenhouse Gas Emission Reduction Credits from Landfill Gas Flaring, City of London W12A Landfill Desktop Review Report The Corporation of the City of London REPORT Submitted to: The Corporation of the City of London 300 Dufferin Avenue, P.O. Box 5035 London, Ontario N6A 4L9 Prepared by: D.H. Lyons Air Quality Management Services 241 Keele Street Toronto, ON M6P 2K1 Project February, 2005

64 Greenhouse Gas Emission Reduction Credits from Landfill Gas Flaring, City of London W12A Landfill Desktop Review Report REPORT Project February 23, 2005 Submitted to: The Corporation of the City of London 300 Dufferin Avenue, P.O. Box 5035 London, Ontario N6A 4L9 Prepared by: Douglas H. Lyons, P.Eng. D.H. Lyons Air Quality Management Services

65 Greenhouse Gas ERCs from Landfill Gas Flaring Desktop Review The Corporation of the City of London Table of Contents Page Summary Basis of Evaluation Scope of Review Information Resources Credentials of Auditor Review of LFG Capture and Control Project Project Summary Emission Reduction Calculations Conclusions...8 D.H.Lyons Page i Feb 2005 Project 05-01

66 Greenhouse Gas ERCs from Landfill Gas Flaring Desktop Review The Corporation of the City of London SUMMARY This project review addresses the requirements for a third party verification audit of greenhouse gas emission reduction credits generated from a landfill gas collection and combustion system under the Pilot Emissions Removals, Reductions and Learnings (PERRL) Initiative. The current document covers the requirements for a Desktop Review Report under the PERRL Verification Protocol (Section 7.0) of the PERRL Proponent s Application Manual, Version 1.0. It is the opinion of the reviewer that the emission reduction credits presented by the proponent are real, measurable and verifiable. Project Scope The project scope accurately defines a valid greenhouse gas reduction activity, with substantiated supporting information. The technical details of the activity changed from the original proposal to the actual installed equipment, however the as built system provides a greater degree of data reliability for the supporting of emission reduction credit calculations than the original proposed system. Emission Reduction Calculations The calculation of the stated Emission Reduction Credits was conducted without error according to accepted standard methodologies. The data used for the performance of the calculations were all derived from reliable sources which were traceable to either a specified manufacturer s performance guarantee or a primary calibration standard. The calculations correctly accounted for periods of operational downtime where no landfill gas flaring was occurring. D.H.Lyons Page 1 Feb 2005 Project 05-01

67 Greenhouse Gas ERCs from Landfill Gas Flaring Desktop Review The Corporation of the City of London 1 BASIS OF EVALUATION 1.1 Scope of Review This project review addresses the requirements for a third party verification audit of greenhouse gas emission reduction credits generated from a landfill gas collection and combustion system under the Pilot Emissions Removals, Reductions and Learnings (PERRL) Initiative. Information provided by the project proponent and associated sub-contractors was assembled and reviewed to ensure the emission reduction credits determined for the project were real, measurable and verifiable. The current document covers the requirements for a Desktop Review Report under the PERRL Verification Protocol (Section 7.0) of the PERRL Proponent s Application Manual, Version 1.0. This review examines the project scope, methodologies, data sources and calculations as undertaken by the project proponent. A technical review of the operation and maintenance of the installed capture and combustion equipment, as required for the Site Visit Report, is provided under a separate cover as a companion to this document. 1.2 Information Resources The performance of the review was undertaken using the following information resources provided directly by the project proponent, the Corporation of the City of London: Proposal Including Scoping Report and Completed Templates for a Landfill Gas Capture and Combustion Project at the W-12A Landfill, City of London, Ontario, dated December 12, 2002 Summary of W12A Landfill Gas Flaring , dated February 23, ER Claim Form Project Data Template MSExcel calculation spreadsheets, compiling raw data obtained from the installed equipment and landfill gas combustion calculations over the operating years 2003 and The following additional information resources were obtained from the subcontractor responsible for installing, operating and maintaining the collection and combustion system: Landfill Gas Collection and Flaring System, list of drawings, August 1, 2004, provided by Comcor Environmental Limited D.H.Lyons Page 2 Feb 2005 Project 05-01

68 Greenhouse Gas ERCs from Landfill Gas Flaring Desktop Review The Corporation of the City of London Technical specifications and operating manuals for continuous flowrate and methane monitoring instrumentation, provided by Comcor Environmental Limited Technical specifications and manufactures performance guarantee for the destruction/removal efficiency of the flare, provided by LFG Specialties, LLC 1.3 Credentials of Auditor All aspects of this audit were conduction by Mr. Douglas Lyons, P.Eng. Mr. Lyons is a licensed professional engineer in the province of Ontario, and has worked as an industrial air quality consultant for more than fifteen years. He has worked with a broad spectrum of industries across Canada and internationally, and maintains specific expertise in the development of air emission inventories, air emission monitoring techniques, continuous emission monitoring systems, air emission mitigation strategies and control technologies. D.H.Lyons Page 3 Feb 2005 Project 05-01

69 Greenhouse Gas ERCs from Landfill Gas Flaring Desktop Review The Corporation of the City of London 2 REVIEW OF LFG CAPTURE AND CONTROL PROJECT 2.1 Project Summary Project Scope The project covers the operation of a landfill gas collection and combustion system operated at the existing W12A landfill by the Corporation of the City of London. The system is described under the original proposal provided by the city to PERRL in December, The system consists of a series of landfill gas extraction wells installed over a closed area of the pre-existing landfill site. The extracted gas is mechanically pumped to a collection station and routed through a flare. A condensate removal system is used to prevent liquid carryover into the collection system and continuous online monitoring is provided for methane concentration, flow rate, oxygen concentration and flare temperature. The control system is designed to maintain the flare combustion at the optimal design conditions, and will vary the flow rate and excess combustion air requirements as needed to maintain a constant combustion profile. Following installation of the landfill gas collection system, a temporary flare was installed during late 2003 to provide some measure of greenhouse gas combustion during construction and commissioning of the permanent installed system for The operational and commissioning history of the system is adequately described in the proponent s summary report for The project as described and installed by the proponent constitutes a recognized and acceptable means of reducing greenhouse gas emissions through the collection and conversion of excess methane generated by the landfill to carbon dioxide. Without the described collection and combustion system, methane generated from the landfill would escape uncontrolled to the atmosphere Emission Reduction Claim The proponent described the baseline scenario of uncontrolled methane emissions according to the accepted PERRL specification using the U.S. EPA LandGEM model. The identification of potential emission reductions were based on the measured methane concentrations and landfill gas flow rates following the collection of the collection and combustion systems. Owing to stated operational and commissioning problems during initial startup, the volumes of landfill gas collected for 2003 and 2004 were given as significantly lower than for the projected future operation of the system. These assumptions are reasonable given the operational data at hand and the proposed future modifications to the system, although any future emission reduction claims would be based on actual measured data for the following years. D.H.Lyons Page 4 Feb 2005 Project 05-01

70 Greenhouse Gas ERCs from Landfill Gas Flaring Desktop Review The Corporation of the City of London 2.2 Emission Reduction Calculations Calculation Methodology The determination of the emission reduction credits for 2003 and 2004 was based on the calculated volume of methane collected and combusted over the operational period. The approach used by the proponent for this calculation is a straight mass balance based on measured operating data from the installed system: M CH4 = DRE V LFG c CH4 ρ CH4 Where, M CH4 = mass flowrate of methane to LFG flare DRE = destruction removal efficiency of flare (99%) V LFG c CH4 ρ CH4 = volume flowrate of LFG to flare at standard conditions = methane concentration (percent by volume) = methane density at standard conditions This is the preferred approach for determining the operational behaviour of the system as it is based to the greatest degree practical on directly measurable data Data Sources The calculation of greenhouse gas emission reduction credits depends on the reliability of three key sources of information: Landfill gas methane concentration; Landfill gas flow rate to flare; and Destruction/Removal efficiency of flare. The methane concentration of the landfill gas is provided continuously by a dedicated continuous emission monitoring system incorporated into the collection system, just downstream of the flare stack. The provision of dedicated, continuous monitoring of methane concentration is a significant improvement in data availability and reliability over the originally proposed system of periodic manual monitoring with a hand held instrument as given under the original project proposal and as recommended by the PERRL Application Manual. During the temporary flare installation, continuous monitoring was provided by a Non-Dispersive Infrared (NDIR) Model 100-IR continuous analyzer, manufactured by California Analytical Instruments Inc. The stated accuracy of the analyzer was given as better than +/- 1% of full scale. For the permanent installation, the D.H.Lyons Page 5 Feb 2005 Project 05-01

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