Landfill methane recovery and destruction (protocol version 2.0)

Foreword

Canada’s Greenhouse Gas (GHG) Offset Credit System is established under Part 2 of the Greenhouse Gas Pollution Pricing Act to provide an incentive to implement projects that result in domestic GHG reductions that would not have been generated in the absence of the project, that go beyond legal requirements and that are not subject to carbon pollution pricing mechanisms.

Canada’s GHG Offset Credit System consists of:

Only projects following a federal offset protocol included in the Compendium and meeting all requirements outlined in the Regulations can generate GHG reductions for which federal offset credits may be issued under the Regulations.

Document revision history
Version number Publication date Summary of changes
2.0 September 9, 2026

The displacement of fossil fuels by eligible landfill gas actively recovered by the project to generate supplemental GHG emission reductions was included in the protocol (Sections 4.3, 8.1.2 and 10.4).

Some elements were added in the reporting (Section 11.0).

Some provisions were clarified or streamlined consistent with the original intent.

1.1 February 24, 2023

The approach for the destruction efficiency values for destruction devices was modified regarding the use of either default values or device-specific values (Section 8.2).

Eligibility is no longer restricted to landfills designed and constructed by landfill cells but is now inclusive of landfills not designed and constructed by landfill cells (Section 4.1).

Some provisions were clarified or streamlined consistent with the original intent.

1.0 June 8, 2022 Initial version of the protocol.

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1.0 Introduction

Methane emissions from landfills are generated by the anaerobic decomposition of organic material in the buried waste. The installation of a landfill gas (LFG) recovery system and an eligible destruction device enables the landfill methane to be converted into biogenic carbon dioxide, instead of allowing it to be passively released to the atmosphere.

The Landfill Methane Recovery and Destruction federal offset protocol is intended for use by a proponent implementing a project that actively recovers LFG and combusts it in an eligible destruction device to generate greenhouse gas (GHG) emission reductions for which federal offset credits may be issued under the Canadian Greenhouse Gas Offset Credit System Regulations (the Regulations). Eligible destruction devices are open and enclosed flares, boilers, turbines, internal combustion engines, stations for the direct injection of upgraded LFG into a natural gas network, and stations for the compression or liquefaction of upgraded LFG prior to its transport and injection into a natural gas network.

The proponent must follow the quantification methodology and requirements set out in this protocol, including those to quantify and report GHG emission reductions generated by eligible project activities. The requirements contained in this protocol are part of the Regulations and must be read in conjunction with provisions in the Regulations.

This protocol is designed to ensure a project generates GHG emission reductions that are real, additional, quantified, verified, unique and permanent. The protocol is also developed in accordance with the principles of ISO 14064-2:2019 Greenhouse gases – Part 2 – Specification with guidance at the project level for quantification, monitoring and reporting greenhouse gas emission reductions or removal enhancements to ensure reported GHG emission reductions generated as a result of implementing a project are relevant, complete, consistent, accurate, transparent, and conservative.

A project that uses actively recovered LFG instead of fossil fuels to produce energy may also generate GHG emission reductions from fossil fuel displacement (that is, fuel switching). However, when the GHG emission reductions are from sources that are subject to a federal or provincial pricing mechanism for GHG emissions, GHG emission reductions from fossil fuel displacement are not additional and are not eligible for federal offset credit issuance.

The proponent is also responsible for ensuring that any GHG emission reductions credited under Canada’s GHG Offset Credit System are unique, that is, they are not credited under another offset program or another GHG reduction mechanism.

2.0 Terms and definitions

Act
means the Greenhouse Gas Pollution Pricing Act.
Active recovery
means the recovery of LFG by a system, which includes gas collection wells, connective piping, blowers, and other technologies, creating a pressure gradient to actively extract LFG.
This does not include passive venting.
Adjacent destruction facility
means a facility adjacent to the landfill site where LFG is combusted and landfill methane (CH4) destroyed in an eligible destruction device.
Biogenic carbon dioxide (CO2)
means CO2 resulting from the decomposition or destruction of organic material, including those produced from the destruction of landfill CH4.
Biogenic CO2 is considered to be part of the natural carbon cycle.
Eligible destruction device
means a device, listed in Table 1, that combusts LFG, destroys landfill CH4 and converts it into biogenic CO2 to generate GHG emission reductions.
Global Warming Potential (GWP)
means a metric representing the ability of a GHG to trap heat in the atmosphere compared to CO2, as set out in Schedule 3 to the Act.
Landfill
means an identifiable area of land where waste is or has been intentionally placed above or below ground for permanent disposal.
Landfill cell
means a unique and discrete section of a landfill designed and constructed to contain a volume of waste.
Landfill gas (LFG)
means a mixture of gases resulting from the decomposition of organic material disposed of in a landfill comprised primarily of landfill CH4, biogenic CO2, and other compounds in low concentrations.
Landfill methane (landfill CH4)
means the CH4 portion of LFG, generated by the anaerobic decomposition of organic material disposed of in a landfill.
Landfill site
means an identifiable area of land where a landfill and all supporting buildings and infrastructure are located.
Project site
means the area of the landfill site from which LFG is actively recovered and the area where it is combusted in the eligible destruction device(s) as part of the project, which may include portions of an adjacent destruction facility.
Regulations
means the Canadian Greenhouse Gas Offset Credit System Regulations.

3.0 Baseline scenario

3.1 Baseline condition

For a project to be eligible under this protocol, the following baseline condition must be met before the project start date:

4.0 Project scenario

4.1 Project conditions

To be eligible under this protocol, a project must meet the following project conditions on and after the project start date:

4.2 Eligible project activities and equipment

Eligible project activities include the:

In cases where an eligible destruction device in a project is located at an adjacent destruction facility, the proponent must have an agreement with the owner of the adjacent destruction facility to ensure that:

Table 1: Eligible destruction devices
Type Description
Open flare A device with a pilot flame at the top of a vertical stack that is exposed to atmosphere that combusts a gas.
Enclosed flare A device with an insulated cylinder stack surrounding a burner manifold and combustion/cooling air louvers that combusts a gas.
Boiler A device that combusts a fuel in order to heat a fluid, such as water or leachate, generating vapour that provides thermal energy for various purposes.
Turbine (micro or large) A device that compresses air to combust with a fuel in order to produce expanding gas that turns turbine blades, generating mechanical energy that can be harnessed by a load (for example, a generator producing electricity).
Internal combustion engine (stationary or mobile) A device that compresses and combusts an air-fuel mixture in a cylinder in order to produce expanding gas that moves a piston and crankshaft, generating rotary mechanical energy that can be harnessed by a load (for example, a generator producing electricity).
Station for direct injection of upgraded LFG into a natural gas networkFootnote 1 A device that monitors and prepares upgraded LFG for injection into a natural gas network; this can include odourizing the gas, metering the flow, regulating the pressure, and monitoring the chemical composition prior to injection.
Station for compression or liquefaction of upgraded LFG prior to transport and injection into a natural gas network A device that compresses or liquefies upgraded LFG for transport to a station for its injection into a natural gas network (see above).

4.3 Eligible LFG for displacement of fossil fuels

LFG actively recovered from within the project site and combusted in an eligible destruction device generating energy may displace fossil fuels. This LFG is eligible to generate GHG emission reductions from the displacement of fossil fuels under this protocol, provided the following conditions are met:

5.0 Additionality

5.1 Legal additionality

GHG emission reductions generated by a project must not occur as a result of federal, provincial or territorial law (including regulations), municipal by-laws, or any other legally binding mandates such as operating permits. This includes legal requirements to recover and combust all or a portion of LFG from the landfill to reduce GHG emissions from the landfill or control of the release of LFG for reasons such as safety precautions (to reduce potential for an explosion) or odour control.

A project at a landfill site with a legal requirement to recover and combust any portion of its LFG is not considered to be additional and, therefore, is not eligible for registration.

If at any time after project registration the GHG emission reductions generated by the project become required by law or the result of a legal requirement, the GHG emission reductions will no longer be additional and, therefore, federal offset credits can only be issued for GHG emission reductions generated up to the date immediately preceding the date on which the law or the legal requirement comes into force.

5.2 Provincial or federal pricing mechanisms for GHG emissions

GHG emission reductions from sources that are subject to a federal or provincial pricing mechanism for GHG emissions are not eligible for federal offset credits. This includes on-site landfills at covered facilities under the federal Output-Based Pricing System.

6.0 General requirements

6.1 Project start date

The start date of a project corresponds to the first day that LFG actively recovered from within the project site is combusted in an eligible destruction device. In the case of the injection of upgraded LFG into a natural gas network, the LFG is considered to be combusted once it is delivered to a station for direct injection or a station for compression or liquefaction.

6.2 Project site location and geographic boundaries

The proponent must document the location and geographic boundaries of the project site and prepare a site plan. The site plan must show:

The geographic boundary of the project site must be established as per the Regulations.

6.3 Environmental and social safeguards

The proponent must ensure that the project activities and the project site comply with any operating permits, municipal by-laws and regulations applicable to the landfill site, including those related to minimizing odour. The proponent must ensure the safe operation of all systems within the project site.

7.0 Project GHG boundary

The project GHG boundary (Figure 1) contains the SSRs that must be included or excluded by the proponent in the baseline and project scenarios to determine the GHG emission reductions generated by the project.

Table 2 provides additional details on the SSRs identified for the baseline and project scenarios, as well as justification for their inclusion or exclusion in the quantification of GHG emission reductions. The proponent must assess each of the “included” SSRs that are relevant to the baseline and project scenarios.

Three GHGs are relevant to the SSRs in this protocol: carbon dioxide (CO2), methane (CH4), and nitrous oxide (N2O). Biogenic CO2 is excluded from the quantification of GHG emission reductions under this protocol, that is biogenic CO2 from SSR 4, SSR 7, SSR 8, SSR 9, SSR 10, SSR 12 and SSR 13.Footnote 2

Figure 1: Illustration of the project GHG boundary

See long description below.
Long description

Figure 1 depicts an illustration of the project GHG boundary. This includes the 13 SSRs relevant to the project type, a dotted line delineating those within the project GHG boundary, and symbols depicting the relationship and connection between SSRs.

SSR 1, SSR 2 and SSR 3 are related to the baseline and project scenarios and are outside the project GHG boundary as the difference between the baseline and project scenarios is assumed to be negligible.

The remaining SSRs are within the project GHG boundary.

SSR 4 is related to the baseline and project scenarios and corresponds to the decomposition of waste materials.

SSR 5 and SSR 6 are related to the project scenario only and correspond to the operation of the project systems and devices and the combustion of supplement fuel to support the operation of a flare.

SSR 7, SSR 8, SSR 9, SSR 10, SSR 12 and SSR 13 are related to the project scenario only and correspond to the combustion of LFG in the various eligible destruction devices under the protocol.

SSR 11 is related to the baseline scenario only and corresponds to the combustion of fossil fuels displaced by LFG.

SSR 1 leads into SSR 2 which leads into SSR 3 which leads into SSR 4 which leads into SSR 5. SSR 5 then leads individually into SSR 7, SSR 8, SSR 9, SSR 10, SSR 12 and SSR 13. SSR 6 leads exclusively into SSR 7. SSR 11 is connected individually to SSR 8, SSR 9 and SSR 10.

Table 2: Details on baseline and project scenario SSRs
SSR Title Description Type Baseline or project scenario GHG Included or excluded
1 Waste materials generation Generation of waste materials before their collection and placement into the landfill. Related Baseline (B1) Project (P1) CO2 Excluded: The difference in GHG emissions between the baseline and project scenarios is assumed to be negligible.
CH4
N2O
2 Waste materials collection Combustion of fossil fuels for vehicles used to collect waste materials and transport them to the landfill site. Related Baseline (B2) Project (P2) CO2 Excluded: The difference in GHG emissions between the baseline and project scenarios is assumed to be negligible.
CH4
N2O
3 Waste materials placement Combustion of fossil fuels to operate equipment for the handling and placement of waste materials into the landfill. Related Baseline (B3) Project (P3) CO2 Excluded: The difference in GHG emissions between the baseline and project scenarios is assumed to be negligible.
CH4
N2O
4 Waste materials decomposition Generation of LFG from the anaerobic decomposition of waste materials in the landfill. Controlled Baseline (B4) CH4 Included: Quantified based on the quantity of landfill CH4 in the LFG actively recovered in the project scenario, using Equation 3.
N2O Excluded: N2O emissions from anaerobic decomposition are not significant.Footnote 3
Project (P4)   CH4 Included: Quantified based on undestroyed landfill CH4 following the combustion of LFG in the eligible destruction device(s), using Equation 12.
N2O Excluded: N2O emissions from anaerobic decomposition are not significant.
5 Operation of LFG recovery system, treatment equipment and destruction devices Combustion of fossil fuels or consumption of grid electricity for the operation of the active LFG recovery system, treatment equipment, and destruction devices.Footnote 4 Fossil Fuels: Controlled   Electricity: Related Project (P5) CO2 Included: Quantified using Equation 9 and Equation 10.
CH4
N2O
6 Supplemental fuel combustion – Flare Combustion of supplemental fossil fuel to support the operation of an open or enclosed flare. Controlled Project (P6) CO2 Included: Quantified based on combustion of supplemental fossil fuel in a flare, using Equation 11.
CH4
N2O
7 LFG combustion – Flare Combustion of LFG in an open or enclosed flare, as identified in Table 1. Controlled Project (P7) CH4 Included: Quantified based on undestroyed landfill CH4 and the generation of N2O from the combustion of LFG in a flare, using Equation 13.
N2O
8 LFG combustion – Boiler Combustion of LFG in a boiler, as identified in Table 1. Controlled Project (P8) CH4 Included: Quantified based on undestroyed landfill CH4 and the generation of N2O from the combustion of LFG in a boiler, using Equation 13.
N2O
9 LFG combustion – Turbine Combustion of LFG in a turbine, as identified in Table 1. Controlled Project (P9) CH4 Included: Quantified based on undestroyed landfill CH4 and the generation of N2O from the combustion of LFG in a turbine, using Equation 13.
N2O
10 LFG combustion– Internal combustion engine Combustion of LFG in an internal combustion engine, as identified in Table 1. Controlled Project (P10) CH4 Included: Quantified based on undestroyed landfill CH4 and the generation of N2O from the combustion of LFG in an internal combustion engine, using Equation 13.
N2O
11 Combustion of fossil fuels displaced by LFG GHG emissions from the combustion of fossil fuels in the baseline scenario that are displaced by eligible LFG recovered in the project scenario Controlled Baseline (B11) CH4 Included: Quantified for fossil fuels displaced by eligible LFG, as per Section 4.3, based on the volume of fossil fuels that would have been needed to produce the amount of energy generated by CH4 from the eligible LFG recovered from within the project site using Equation 6 .
N2O
12 LFG combustion – Natural gas network direct injection Combustion of upgraded LFG after its direct injection into a natural gas network, as identified in Table 1. Related Project (P12) CH4 Included: Quantified based on undestroyed landfill CH4 and the generation of N2O from the combustion of LFG after its direct injection into a natural gas network, using Equation 13.
N2O
13 LFG combustion – Compression or liquefaction for natural gas network injection Combustion of upgraded LFG after its compression or liquefaction, transport and injection into a natural gas network, as identified in Table 1. Related Project (P13) CH4 Included: Quantified based on undestroyed landfill CH4 and the generation of N2O from the combustion of LFG after its compression or liquefaction, transport and injection into a natural gas network, using Equation 13.
N2O

8.0 Quantification methodology

This section contains the quantification methodology that the proponent must follow to quantify baseline and project scenario GHG emissions and subsequently, the GHG emission reductions generated by the project.

Baseline scenario GHG emissions are the GHG emissions from the SSRs within the project GHG boundary that would likely have been generated in the absence of the project from the business-as-usual management and operation of the landfill, and quantified as per Section 8.1.

Project scenario GHG emissions are the GHG emissions from the SSRs within the project GHG boundary that are generated from the eligible project activities and quantified as per Section 8.2.

The GHG emission reductions generated by the project are quantified by deducting the project scenario GHG emissions from the baseline scenario GHG emissions as per Section 8.4.

The quantification of both the baseline and project scenario GHG emissions must include all the GHG emissions that were likely to occur in the absence of the project (baseline scenario) and did occur (project scenario) during a reporting period. The proponent must report the sub-totals in tonnes of CO2 equivalent (t CO2e) for each full or partial calendar year of the reporting period to support issuance of the offset credits by calendar year.

For an aggregation of projects, the proponent must quantify GHG emission reductions for each project separately. Subsequently, the GHG emission reductions for each project are to be summed together to determine the GHG emission reductions for the aggregation of projects. The proponent must report the sub-totals of each project within the aggregation in tonnes of CO2 equivalent (t CO2e) for each full or partial calendar year of the reporting period to support issuance of the offset credits by calendar year.

Some emission factors and other reference values used in the quantification methodology are provided in the Emission Factors and Reference Values document.Footnote 5 Raw data must be converted to align with the units presented in the quantification methodology, if necessary.

8.1 Baseline scenario GHG emissions

The proponent must use Equation 1 and the subsequent equations in Section 8.1 to quantify the baseline scenario GHG emissions for each full or partial calendar year covered by the reporting period, based on the included SSRs as set out in Table 2.

The baseline scenario GHG emissions are quantified using of a dynamic baseline approach based on measurements made in the project scenario instead of modelling the GHG emissions generated by the landfill in the baseline scenario. This means that the baseline scenario GHG emissions are quantified based on the quantity of landfill CH4 in the LFG that is actively recovered in the project scenario, which may vary over time.

Equation 1: Baseline scenario GHG emissions for a calendar year covered by the reporting period

BE C = BLE C + FDE C

Parameter Description Units

BEC

Baseline scenario GHG emissions for a calendar year covered by the reporting period t CO2e
BLEC Baseline scenario CH4 emissions from the landfill for a calendar year covered by the reporting period, as per Equation 2 t CO2e
FDEC Baseline scenario GHG emissions from the combustion of fossil fuels displaced by eligible LFG for a calendar year covered by the reporting period, as per Equation 6 (SSR B11) t CO2e
C Calendar year unitless

8.1.1 Baseline scenario CH4 emissions from the landfill

The proponent must use Equation 2 to quantify the baseline scenario CH4 emissions from the landfill for a calendar year covered by the reporting period.

Equation 2: Baseline scenario CH4 emissions from the landfill for a calendar year covered by the reporting period

BLE C = CH 4 REC C × ( 1 OX )

Parameter Description Units
BLEC Baseline scenario CH4 emissions from the landfill for a calendar year covered by the reporting period t CO2e
CH4RECC Quantity of landfill CH4 in the LFG actively recovered for a calendar year covered by the reporting period, as per Equation 3 (SSR B4) t CO2e
OX Factor for the oxidation of landfill CH4 by bacteria in soil or materials covering the waste, as determined below unitless
C Calendar year unitless

Baseline scenario GHG emissions are quantified based on the presumption that the LFG actively recovered in the project scenario would have been passively released to the atmosphere in the baseline scenario. Oxidation of landfill CH4 must be accounted for in the baseline scenario. If a non-geomembrane cover system or other CH4 oxidation technology is present, it can be presumed that the landfill CH4 would have been subject to oxidation by bacteria in the soil or materials covering the waste prior to being released to the atmosphere. If a geomembrane covers the entire landfill area and no CH4 oxidation technology is present, it can be presumed that the landfill CH4 would not have been subject to oxidation.

Oxidation of landfill CH4 must be accounted for in the following manner:

The proponent must use Equation 3 and Equation 4 to quantify the quantity of landfill CH4 in the LFG that is actively recovered for each full or partial calendar year covered by the reporting period.

Equation 3: Quantity of landfill CH4 in the LFG actively recovered for a calendar year covered by the reporting period

CH 4 REC C = i n Q i × ρ CH 4 1000 × GWP CH 4

Parameter Description Units
CH4RECC Quantity of landfill CH4 in the LFG actively recovered for a calendar year covered by the reporting period (SSR B4) t CO2e
Qi Volume of landfill CH4 delivered to eligible destruction device, i, during a calendar year covered by the reporting period, as per Equation 4 m3 CH4
ρCH4 Reference density of CH4 = 0.656 kg CH4/m3 CH4
GWPCH4 GWP of CH4, as set out in Schedule 3 to the Act unitless
1000 Conversion factor, kilograms to tonnes kg/t
n Number of eligible destruction devices unitless
i Eligible destruction device unitless
C Calendar year unitless

Equation 4: Volume of landfill CH4 delivered to an eligible destruction device for a calendar year covered by the reporting period

Q i = t n ( LFG i , t × LFG CH 4 , t )

Parameter Description Units
Qi Volume of landfill CH4 delivered to eligible destruction device, i, during a calendar year covered by the reporting period m3 CH4
LFGi,t Corrected volume of LFG delivered to eligible destruction device, i, during measurement period, t, as per automatic correction or Equation 5 m3 LFG
LFGCH4,t Average CH4 content of the LFG during measurement period, t m3 CH4/m3 LFG
i Eligible destruction device unitless
n Number of measurement periods in a calendar year covered by the reporting period unitless
t Measurement period unitless

All flow meter data must be corrected to the reference temperature and pressure conditions. If the flow meter does not automatically correct the measured volume to the reference temperature and pressure conditions, the proponent must quantify the corrected volume following Equation 5. Equation 5 is not needed if the flow meter automatically corrects the volume.

Equation 5: Volume of LFG delivered to an eligible destruction device, corrected to reference conditions

LFG i , t = LFG UC , i , t × T ref T i , t × P i , t P ref

Parameter Description Units
LFGi,t Corrected volume of LFG delivered to eligible destruction device, i, during measurement period, t m3 LFG
LFGUC,i,t Uncorrected volume of LFG delivered to eligible destruction device, i, during measurement period, t m3 LFG
Ti,t Measured temperature of the LFG delivered to eligible destruction device, i, for the measurement period, t K
Tref Reference temperature of the LFG = 298.15 K K
Pi,t Measured pressure of the LFG delivered to eligible destruction device, i, for the measurement period, t kPa
Pref Reference pressure of the LFG = 101.325 kPa kPa
i Eligible destruction device unitless
t Measurement period unitless

8.1.2 Baseline scenario GHG emissions from the combustion of fossil fuels displaced by eligible LFG

If the project actively recovers and combusts LFG eligible for the displacement of fossil fuels and the proponent chooses to quantify the resulting GHG emission reductions for credit issuance, they must use Equation 6 to quantify baseline scenario GHG emissions from the combustion of fossil fuels displaced by eligible LFG.

Equation 6: Baseline scenario GHG emissions from combustion of fossil fuels displaced by eligible LFG for a calendar year covered by the reporting period

FDE C = i n [ ( FD i , C × EF CO 2 , i ) + ( FD i , C × EF CH 4 , i × GWP CH 4 ) + ( FD i , C × EF N 2 O , i × GWP N 2 O ) ] ÷ 1000

Parameter Description Units
FDEC Baseline scenario GHG emissions from the combustion of fossil fuels displaced by eligible LFG for a calendar year covered by the reporting period (SSR B11) t CO2e
FDi,C Volume of fossil fuel, i, displaced by eligible LFG and used in the baseline scenario for a calendar year covered by the reporting period, as per Equation 7 m3
EFCO2,i CO2 emission factor for fossil fuel, i, as set out in the Emission Factors and Reference Values document kg CO2/m3
EFCH4,i CH4 emission factor for fossil fuel, i, as set out in the Emission Factors and Reference Values document kg CH4/m3
GWPCH4 GWP of CH4, as set out in Schedule 3 to the Act unitless
EFN2O,i N2O emission factor for fossil fuel, i, as set out in the Emission Factors and Reference Values document kg N2O/m3
GWPN2O GWP of N2O, as set out in Schedule 3 to the Act unitless
1000 Conversion factor, kilograms to tonnes kg/t
n Number of eligible fossil fuels displaced by eligible LFG unitless
i Fossil fuel displaced by eligible LFG unitless
C Calendar year unitless

The volume of fossil fuels that would have been used in the baseline scenario (FDi,C) to generate the equivalent amount of energy as the combustion of eligible LFG must be calculated using Equation 7. However, if the value of FDi,C, obtained from Equation 7, is higher than the highest annual volume of fossil fuels used during the 3 years before the project start date, the proponent must use the highest annual volume of fossil fuel as the value of FDi,C in Equation 6.

Equation 7: Volume of fossil fuels displaced by eligible LFG for a calendar year covered by the reporting period

FD i , C = LFD C × ( HHV LFG HHV FF , i )

Parameter Description Units
FDi,C Volume of fossil fuel, i, displaced by eligible LFG and used in the baseline scenario for a calendar year covered by the reporting period m3
LFDC Volume of LFG eligible for displacement of fossil fuels in the project scenario for a calendar year covered by the reporting period m3
HHVLFG Higher heating value (HHV) of LFG actively recovered from within the project site, as set out in the Emission Factors and Reference Values document MJ/m3
HHVFF,i HHV of fossil fuel, i, displaced by eligible LFG, as set out in the Emission Factors and Reference Values document MJ/m3
i Fossil fuel displaced by eligible LFG unitless
C Calendar year unitless

If eligible LFG has been upgraded to the standards required to be RNG, the proponent must use the applicable higher heating value for RNG, as set out in the Emission Factors and Reference Values document, for the parameter HHVLFG in Equation 7.

If eligible LFG has not been upgraded to the standards required to be RNG, the proponent must use the higher heating value for biogas regardless of the CH4 composition of the biogas, as set out in the Emission Factors and Reference Values document, for the parameter HHVLFG in Equation 7.

Despite the previous provision, the proponent may determine a project-specific higher heating value for eligible LFG by measuring the energy density of the LFG following the requirements for fuel heat content monitoring set out in Section 2.D.3 of the latest available version of Canada’s Greenhouse Gas Quantification Requirements / Greenhouse Gas Reporting Program, and corrected to standard conditions.

8.2 Project scenario GHG emissions

The proponent must use Equation 8 and the subsequent equations in Section 8.2 to quantify the project scenario GHG emissions for each full or partial calendar year covered by the reporting period, based on the included SSRs, as set out in Table 2.

The project scenario GHG emissions correspond to the GHG emissions from, as applicable:

Equation 8: Project scenario GHG emissions for a calendar year covered by the reporting period

PE C = FF GHG + EL GHG + FF flare , GHG + LFG GHG

Parameter Description Units
PEC Project scenario GHG emissions for a calendar year covered by the reporting period t CO2e
FFGHG GHG emissions from the use of fossil fuels for the operation of the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period, as per Equation 9 (SSR P5) t CO2e
ELGHG GHG emissions from the use of grid electricity for the operation of the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period, as per Equation 10 (SSR P5) t CO2e
FFflare,GHG GHG emissions from the use of supplemental fossil fuels to support the operation of a flare for a calendar year covered by the reporting period, as per Equation 11 (SSR P6) t CO2e
LFGGHG GHG emissions from the combustion of LFG in the eligible destruction device(s) for a calendar year covered by the reporting period, as per Equation 13 (SSR P7, SSR P8, SSR P9, SSR P10, SSR P12, SSR P13) t CO2e
C Calendar year unitless

Equation 9 and Equation 10 quantify the GHG emissions from the operation of the active LFG recovery system, treatment equipment, and destruction devices for each full or partial calendar year covered by the reporting period, which correspond to SSR P5. The proponent must use the appropriate equation(s) dependent on the energy inputs required for the operation of the active LFG recovery system, treatment equipment, and destruction devices; these can include blowers, equipment for LFG treatment and purification, destruction devices (other than flares), equipment for the conveyance of LFG to an adjacent destruction facility, and/or equipment for the upgrading, compression or liquefaction, and injection of upgraded LFG into a natural gas network. If both fossil fuels and grid electricity are used for these purposes, the proponent must use the summation of Equation 9 and Equation 10 to quantify SSR P5.

Equation 9: GHG emissions from the combustion of fossil fuels for the operation of the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period

FF GHG = j m [ ( FF j × EF CO 2 , j ) + ( FF j × EF CH 4 , j × GWP CH 4 ) + ( FF j × EF N 2 O , j × GWP N 2 O ) ] ÷ 1000

Parameter Description Units
FFGHG GHG emissions from the combustion of fossil fuels for the operation of the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period (SSR P5) t CO2e
FFj Volume of fossil fuel, j, consumed by the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period m3
EFCO2,j CO2 emission factor for fossil fuel, j, as set out in the Emission Factors and Reference Values document kg CO2/m3
EFCH4,j CH4 emission factor for fossil fuel, j, as set out in the Emission Factors and Reference Values document kg CH4/m3
GWPCH4 GWP of CH4, as set out in Schedule 3 to the Act unitless
EFN2O,j N2O emission factor for fossil fuel, j, as set out in the Emission Factors and Reference Values document kg N2O/m3
GWPN2O GWP of N2O, as set out in Schedule 3 to the Act unitless
1000 Conversion factor, kilograms to tonnes kg/t
m Number of types of fossil fuels unitless
j Type of fossil fuel unitless

Equation 10: GHG emissions from the use of grid electricity for the operation of the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period

EL GHG = EL × EF EL , GHG 1000

Parameter Description Units
ELGHG GHG emissions from the use of grid electricity for the operation of the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period (SSR P5) t CO2e
EL Grid electricity consumed by the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period MWh
EFEL,GHG Emission factor for the electricity consumption GHG emission intensity for the grid of the project’s province or territory, as set out in the Emission Factors and Reference Values document kg CO2e/MWh
1000 Conversion factor, kilograms to tonnes kg/t

If the project includes a flare as a destruction device, the proponent must use Equation 11 to quantify the GHG emissions from supplemental fossil fuels used to support the operation of a flare for each full or partial calendar year covered by the reporting period, which corresponds to SSR P6.

Equation 11: GHG emissions from the combustion of supplemental fossil fuels to support the operation of a flare for a calendar year covered by the reporting period

FF flare , GHG = j m [ ( FF flare , j × EF CO 2 , j ) + ( FF flare , j × FF CH 4 , j × ρ CH 4 × ( 1 DE CH 4 ) × GWP CH 4 ) + ( FF flare , j × EF N 2 O , j × GWP N 2 O ) ] ÷ 1000

Parameter Description Units
FFflare,GHG GHG emissions from the combustion of supplemental fossil fuels to support the operation of a flare for a calendar year covered by the reporting period (SSR P6) t CO2e
FFflare,j Volume of supplemental fossil fuel, j, consumed by a flare for a calendar year covered by the reporting period m3
EFCO2,j CO2 emission factor for supplemental fossil fuel, j, as set out in the Emission Factors and Reference Values document kg CO2/m3
FFCH4,j Average CH4 content of supplemental fossil fuel, j, obtained from the supplier m3 CH4/m3
ρCH4 Reference density of CH4 = 0.656 kg CH4/m3 CH4
DECH4 CH4 destruction efficiency of the flare, as set out in the Emission Factors and Reference Values document or specific to the device unitless
GWPCH4 GWP of CH4, as set out in Schedule 3 to the Act unitless
EFN2O,j N2O emission factor for supplemental fossil fuel, j, as set out in the Emission Factors and Reference Values document kg N2O/m3
GWPN2O GWP of N2O, as set out in Schedule 3 to the Act unitless
1000 Conversion factor, kilograms to tonnes kg/t
m Number of types of supplemental fossil fuels unitless
j Type of supplemental fossil fuel unitless

The proponent must use Equation 12 and Equation 13 to quantify GHG emissions due to the combustion of LFG in the eligible destruction device(s) for each full or partial calendar year covered by the reporting period. Equation 12 determines the undestroyed landfill CH4 generated from the anaerobic decomposition of waste and released to atmosphere from the eligible destruction device(s), corresponding to SSR P4. This value is then accounted for within Equation 13, which must be used to quantify the quantity of undestroyed landfill CH4 and generated N2O emissions from the combustion of LFG in the eligible destruction device(s) for each full or partial calendar year covered by the reporting period, corresponding to SSR P7, SSR P8, SSR P9, SSR P10, SSR P12, and SSR P13.

Equation 12: Undestroyed landfill CH4 released to atmosphere based on the destruction efficiency of the eligible destruction device(s) for a calendar year covered by the reporting period

CH 4 UND = i n [ Q i × ( 1 DE CH 4 , i ) ] × ρ CH 4 1000 × GWP CH 4

Parameters Description Units
CH4UND Undestroyed landfill CH4 released to atmosphere based on the destruction efficiency of the eligible destruction device(s) for a calendar year covered by the reporting period (SSR P4) t CO2e
Qi Volume of landfill CH4 delivered to eligible destruction device, i, during a calendar year covered by the reporting period, as per Equation 4 m3 CH4
DECH4,i CH4 destruction efficiency of eligible destruction device, i, as set out in the Emission Factors and Reference Values document or specific to the device unitless
ρCH4 Reference density of CH4 = 0.656 kg CH4/m3 CH4
GWPCH4 GWP of CH4, as set out in Schedule 3 to the Act unitless
1000 Conversion factor, kilograms to tonnes kg/t
n Number of eligible destruction devices unitless
i Eligible destruction device unitless

The amount of landfill CH4 destroyed in each eligible destruction device is dependent on the CH4 destruction efficiency for each device (DECH4). The Emission Factors and Reference Values document sets out default CH4 destruction efficiencies that the proponent must use for each eligible destruction device in the project.

Despite the previous provision, the proponent may determine a device-specific destruction efficiency for each eligible destruction device in the project. Testing for the device-specific destruction efficiency must be conducted each full or partial calendar year, and include at least three test runs, with the accepted final value being one standard deviation below the mean of the measured efficiencies.

Equation 13: GHG emissions from the destruction of LFG in the eligible destruction device(s) for a calendar year covered by the reporting period

LFG GHG = CH 4 UND + [ i n ( Q i × EF LFG , N 2 O , i 1000 ) × ρ CH 4 1000 × GWP N 2 O ]

Parameter Description Units
LFGGHG GHG emissions from the destruction of LFG in the eligible destruction device(s) for a calendar year covered by the reporting period (SSR P7, SSR P8, SSR P9, SSR P10, SSR P12, SSR P13) t CO2e
CH4UND Undestroyed landfill CH4 released to atmosphere based on the destruction efficiency of the eligible destruction device(s) for a calendar year covered by the reporting period, as per Equation 12 (SSR P4) t CO2e
Qi Volume of landfill CH4 delivered to eligible destruction device, i, during a calendar year covered by the reporting period, as per Equation 4 m3 CH4
ρCH4 Reference density of CH4 = 0.656 kg CH4/m3 CH4
EFLFG,N2O,i N2O emission factor for the destruction of LFG in eligible destruction device, i, as set out in the Emission Factors and Reference Values document kg N2O/t CH4
1000 Conversion factor, kilograms to tonnes kg/t
GWPN2O GWP of N2O, as set out in Schedule 3 to the Act unitless
n Number of eligible destruction devices unitless
i Eligible destruction device unitless

8.3 Leakage

While waste could be diverted away from a landfill site due to increased costs or tipping fees resulting from the implementation of a project, which would cause the landfill CH4 emissions to be passively released to the atmosphere elsewhere, the high costs associated with collecting and transporting this waste to a farther location are presumed to render this leakage scenario improbable.

As a result, leakage was determined to be inapplicable to this project type and there is no leakage discount factor (which corresponds to variable Ci in the formula in subsection 20(2) of the Regulations) to be applied for the quantification of GHG emission reductions generated by a project implemented following this protocol.

8.4 Project GHG emission reductions

The proponent must use Equation 14 to quantify the GHG emission reductions (ERC) generated by the project, which correspond to the GHG reductions determined in accordance with section 20 of the Regulations.

Equation 14: Project GHG emission reductions for a calendar year covered by the reporting period

ER C = BE C PE C

Parameter Description Units
ERC Project GHG emission reductions for a calendar year covered by the reporting period t CO2e
BEC Baseline scenario GHG emissions for a calendar year covered by the reporting period, as per Equation 1 t CO2e
PEC Project scenario GHG emissions for a calendar year covered by the reporting period, as per Equation 8 t CO2e
C Calendar year unitless

9.0 Measurement and data

9.1 Measuring devices

The proponent must ensure the appropriate measuring devices are installed and operated as per the requirements in Section 9.1.

9.1.1 Flow meters

The proponent must ensure that permanent flow meters directly and separately measure the volume of LFG actively recovered from within the project site and delivered to the individual eligible destruction device(s). The volume of any fossil fuels consumed for the operation of the active LFG recovery system, treatment equipment, or eligible destruction devices must be measured by permanent flow meters or determined using purchasing records. Volume data must be converted into cubic metres (m3) to align with the quantification methodology presented in Section 8.0.

9.1.2 Temperature and pressure gauges

If a flow meter automatically corrects the LFG volume to the reference temperature and pressure conditions set out in Equation 5, no additional temperature and pressure gauges are required.

If a flow meter does not automatically correct the LFG volume, permanent temperature and pressure gauges must be installed to measure temperature and pressure at the same measurement frequency as the uncorrected volume of LFG (Section 9.2). LFG temperature and pressure must be measured under the same conditions (wet or dry basis) as the LFG volume.

The LFG volume data must be corrected from measured temperature and pressure conditions to the reference temperature and pressure conditions using Equation 5.

9.1.3 Methane analyzers

The active LFG recovery system must include permanent methane analyzers (for example, gas chromatographs) that directly measure the CH4 content in the LFG on a volumetric basis.

9.1.4 Arrangement of measuring devices

Flow meters and methane analyzers must be arranged in such a way as to ensure the data is representative of the LFG actively recovered by the project.

Additionally, flow meters and methane analyzers must be placed to:

Measuring devices should be arranged such that the CH4 content of the LFG is measured under the same conditions (wet or dry basis) as the volume, temperature and pressure. However, a moisture-removing component may separate a methane analyzer and a flow meter where the methane analyzer is placed upstream of the moisture-removing component (CH4 content measured on a wet basis), and the flow meter is placed downstream of the moisture-removing component (LFG volume measured on a dry basis). A moisture-removing component must not separate a methane analyzer and flow meter in any other configuration other than previously described. No other devices or equipment that could change the LFG composition by volume may separate a methane analyzer and a flow meter.

9.2 Measurement method and frequency

Table 3 identifies the parameters in the quantification methodology set out in Section 8.0 that must be measured and provides details regarding measurement method and frequency.

Table 3: Measurement method and frequency for measured parameters
Parameter Description Units Measurement method and frequency Equations
LFGi,t Corrected volume of LFG delivered to eligible destruction device, i, during measurement period, t. m3 LFG

Measured continuously with volume recorded every measurement period. The measurement period can be a maximum of 15 minutes.

or

Quantified as per Equation 5 if flow meter does not automatically correct volume.

4, 5
LFGCH4,t Average CH4 content of the LFG during measurement period, t. m3 CH4/m3 LFG Measured continuously with CH4 content averaged over the measurement period. The measurement period can be a maximum of 15 minutes. 4
LFGUC,i,t Uncorrected volume of LFG delivered to eligible destruction device, i, during measurement period, t. m3 LFG Measured continuously with volume recorded every measurement period. The measurement period can be a maximum of 15 minutes. 5
Ti,t Measured temperature of the LFG for the measurement period, t. K Measured continuously with value recorded every measurement period if flow meter does not automatically correct volume. The measurement period can be a maximum of 15 minutes but must be the same frequency as for LFGUC,i,t. 5
Pi,t Measured pressure of the LFG for the measurement period, t. kPa Measured continuously with value recorded every measurement period if flow meter does not automatically correct volume. The measurement period can be a maximum of 15 minutes but must be the same frequency as for LFGUC,i,t. 5
LFDC Volume of LFG eligible for displacement of fossil fuels in the project scenario for a calendar year covered by the reporting period. m3

Measured continuously with volume recorded every measurement period. The measurement period can be a maximum of 15 minutes.

or

Quantified as per Equation 5 if flow meter does not automatically correct volume.

7
FFj Volume of fossil fuel, j, consumed by the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period. m3

Measured continuously with volume recorded at least once every 15 minutes and summed for each calendar year covered by the reporting period.

or

Calculated from fossil fuel purchasing records and/or equipment specifications and summed for each calendar year covered by the reporting period.

9
EL Grid electricity consumed by the active LFG recovery system, treatment equipment, and destruction devices for a calendar year covered by the reporting period. MWh

Measured using meter and summed for each calendar year covered by the reporting period.

or

Calculated from electricity purchasing records and/or equipment specifications and summed for each calendar year covered by the reporting period.

10
FFflare,j Volume of supplemental fossil fuel, j, consumed by a flare for a calendar year covered by the reporting period. m3

Measured continuously with volume recorded at least once every 15 minutes and summed for each calendar year covered by the reporting period.

or

Calculated from fossil fuel purchasing records and/or equipment specifications and summed for each calendar year covered by the reporting period.

11

9.3 Quality assurance and quality control

The proponent must have documented quality assurance and quality control (QA/QC) procedures and must implement them to ensure that all measurements and calculations are made in accordance with this protocol and can be verified.

All flow meters and methane analyzers must be:

The measurement accuracy of all measuring devices must be within a ± 5% accuracy range. When the measurement accuracy of a measuring device exceeds the ± 5% range, the appropriate corrective actions must be taken on the device, in accordance with the manufacturer specifications. 

After the corrective actions, the measuring device must be rechecked for accuracy. If the measurement accuracy of the measuring device is still not within the ± 5% range, the measuring device must be calibrated by the manufacturer or by a third party certified for that purpose and following manufacturer specifications, no more than 2 months after the accuracy check conducted following the corrective actions. If the measuring device was manufactured with no possibility of calibration, it must be replaced no more than 2 months after the accuracy check conducted following the corrective actions.

When the measurement accuracy of a measuring device indicates a reading outside of a ± 5% accuracy range, the following conditions must be followed for the entire period from the last time the measuring device showed a reading within ± 5% accuracy until the measuring device shows a return to ± 5% accuracy:

9.4 Missing data

If a measuring device fails to produce data as required in Section 9.2, missing data may be substituted following the requirements in this section. If missing data cannot be substituted as per the applicable requirements, no GHG emission reductions can be quantified for the issuance of offset credits for the period during which data is missing.

Missing data from a measuring device may only be substituted if the following two conditions are met during the period of missing data:

Missing data from a flow meter or methane analyzer may only be substituted in accordance with the following rules:

For a project with LFG volume or CH4 content data missing for a period of up to 7 consecutive days, the proponent must use the appropriate substitution method set out in Table 4 to substitute the data.

For data missing for more than 7 consecutive days, only the data for the period of up to 7 days may be substituted. No data may be substituted for the period after the 7th consecutive day, and no GHG emission reductions may be quantified for the issuance of offset credits for that period.

Table 4: Missing data substitution methods
Missing data period Substitution method
Less than 6 consecutive hours Use the average of the 4 hours immediately prior to and after the missing data period.
6 to less than 24 consecutive hours Use the 95% upper or lower confidence limit of the 72 hours prior to or after the missing data period, whichever results in greater conservativeness.
1 to 7 consecutive days Use the 90% upper or lower confidence limit of the 72 hours prior to or after the missing data period, whichever results in greater conservativeness.

In the event that periods of missing data occur more than once during the reporting period, data may be substituted to quantify:

9.5 Operational status of eligible destruction devices

The operational status of the eligible destruction device(s) must be monitored with a destruction device monitoring instrument and recorded at least hourly to ensure LFG combustion is occurring.

For a flare (open or enclosed), the operational status must be determined based on data from a thermocouple. The thermocouple must indicate that the flare temperature meets or exceeds 260°C, the minimum temperature for CH4 destruction. If the temperature is below 260°C, no GHG emission reductions can be quantified for the period during which the temperature remains below 260°C.

For all other eligible destruction devices listed in Table 1, the destruction device monitoring instrument must monitor and measure an indicator of operational status appropriate for the destruction device such as energy output. If the operational status is not monitored and an indicator is not measured, no GHG emission reductions can be quantified for the period during which monitoring data is not measured.

In cases where LFG is combusted in an eligible destruction device located at an adjacent destruction facility, monitoring data demonstrating the operational status of the eligible destruction device must be made available to the proponent, otherwise the GHG emission reductions can not be included in the quantification.

If an eligible destruction device, thermocouple or other destruction device monitoring instrument is not operating or functioning properly in accordance with the manufacturer specifications, no GHG emission reductions can be quantified for the period during which they are not operating or functioning properly.

10.0 Records

In addition to the record keeping requirements specified in the Regulations, the proponent must keep records of all data and information that support the implementation of the project and verification, including invoices, contracts, metered results, maintenance records, calculations, databases, photographs, and calibration records. The records must be kept and retained at the location and for the period of time specified in the Regulations. These records requirements apply to the entire project site, including the landfill site and any adjacent destruction facility, all project activities, eligible destruction devices, measuring devices or meters and monitoring instruments, as applicable.

10.1 Project site

The proponent must keep a record of the information about the project site, including:

10.2 Project activities

The proponent must keep a record of the information about the project activities, including:

10.3 Eligible destruction devices

The proponent must keep a record of the information about the eligible destruction device(s) including:

10.4 Displacement of fossil fuels

If applicable, the proponent must keep a record of the information about the displacement of fossil fuels by eligible LFG, as per Section ‎3.1 and Section ‎4.3, including:

10.5 Measuring devices and other equipment

The proponent must keep a record of the information about the measuring devices and other equipment in the project, including:

10.6 Quantification

The proponent must keep a record of all information and data used to support the quantification of the GHG emission reductions including:

11.0 Reporting

In addition to the reporting requirements specified in the Regulations, the proponent must include the following in project reports.

In the initial project report, the proponent must include:

In any project report, the proponent must include:

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2026-09-09