ࡱ> lq` 0{}bjbjqPqP 8::Z rbbb"dIdIdI8I@K0TJzV(VLVVY [[X$h\YY\\VV lll\ VVl\llsl*V$T GXdI0aߘ@+̽0~bp ~T6~H\\l\\\\\`ld\\\\\\\d<dę< Approved consolidated baseline methodology ACM0001 Consolidated baseline and monitoring methodology for landfill gas project activities I. SOURCE AND APPLICABILITY Sources This consolidated baseline and monitoring methodology is based on elements from the following approved baseline and monitoring methodologies: AM0002: Greenhouse Gas Emission Reductions through Landfill Gas Capture and Flaring where the Baseline is established by a Public Concession Contract (approved based on proposal NM0004rev: Salvador da Bahia landfill gas project, whose project design document and baseline study, monitoring and verification plans were developed by ICF Consulting (version 03, June2003); AM0003: Simplified financial analysis for landfill gas capture projects (approved based on proposal NM0005: Nova Gerar landfill gas to energy project, whose project design document and baseline study, monitoring and verification plans were developed by EcoSecurities Ltd. (version 14, July 2003) for the Carbon Finance Unit of the World Bank); AM0010: Landfill gas capture and electricity generation projects where landfill gas capture is not mandated by law (approved based on proposal NM0010-rev: Durban-landfill-gas-to-electricity project, whose project design document and baseline study, monitoring and verification plans were developed by Prototype Carbon Fund of the World Bank (April 2003); AM0011: Landfill gas recovery with electricity generation and no capture or destruction of methane in the baseline scenario (approved based on proposal NM0021: Cerupt methodology for landfill gas recovery, whose project design document and baseline study, monitoring and verification plans were developed by Onyx (July 2003). The methodology also refers to the latest approved version of the following tools: Tool for the demonstration and assessment of additionality; Tool to determine project emissions from flaring gases containing methane; Tool to calculate baseline, project and/or leakage emissions from electricity consumption; Tool to calculate project or leakage CO2 emissions from fossil fuel combustion; Combined tool to identify the baseline scenario and demonstrate additionality; Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal site; Tool to calculate the emission factor for an electricity system. For more information regarding the approved methodologies and the tools as well as their consideration by the Executive Board please refer to < HYPERLINK "http://cdm.unfccc.int/goto/MPappmeth" http://cdm.unfccc.int/goto/MPappmeth>. Selected approach from paragraph 48 of the CDM modalities and procedures Emissions from a technology that represents an economically attractive course of action, taking into account barriers to investment. Applicability This methodology is applicable to landfill gas capture project activities, where the baseline scenario is the partial or total atmospheric release of the gas and the project activities include situations such as: The captured gas is flared; and/or The captured gas is used to produce energy (e.g. electricity/thermal energy). Emission reductions can be claimed for thermal energy generation, only if the LFG displaces use of fossil fuel either in a boiler or in an air heater. For claiming emission reductions for other thermal energy equipment (e.g. kiln), project proponents may submit a revision to this methodology; The captured gas is used to supply consumers through natural gas distribution network. If emissions reductions are claimed for displacing natural gas, project activities may use approved methodology AM0053. In addition, the applicability conditions included in the tools referred to above apply. II. BASELINE METHODOLOGY Project Boundary The project boundary is the site of the project activity where the gas is captured and destroyed/used. If the electricity for project activity is sourced from grid or electricity generated by the LFG captured would have been generated by power generation sources connected to the grid, the project boundary shall include all the power generation sources connected to the grid to which the project activity is connected. If the electricity for project activity is from a captive generation source or electricity generated by the captured LFG would have been generated by a captive power plant, the captive power plant shall be included in the project boundary. Table 1: Summary of gases and sources included in the project boundary and justification/explanation where gases and sources are not included SourceGasIncluded?Justification / ExplanationBaselineEmissions from decomposition of waste at the landfill siteCH4YesThe major source of emissions in the baselineN2ONoN2O emissions are small compared to CH4 emissions from landfills. Exclusion of this gas is conservative.CO2NoCO2 emissions from the decomposition of organic waste are not accountedEmissions from electricity consumptionCO2YesElectricity may be consumed from the grid or generated onsite/offsite in the baseline scenarioCH4NoExcluded for simplification. This is conservative.N2ONoExcluded for simplification. This is conservative.Emissions from thermal energy generationCO2YesIf thermal energy generation is included in the project activityCH4NoExcluded for simplification. This is conservative.N2ONoExcluded for simplification. This is conservative.Project ActivityOn-site fossil fuel consumption due to the project activity other than for electricity generationCO2YesMay be an important emission source CH4NoExcluded for simplification. This emission source is assumed to be very small.N2ONoExcluded for simplification. This emission source is assumed to be very small.Emissions from on-site electricity useCO2YesMay be an important emission sourceCH4NoExcluded for simplification. This emission source is assumed to be very small.N2ONoExcluded for simplification. This emission source is assumed to be very small.Procedure for the selection of the most plausible baseline scenario Step 1: Identification of alternative scenarios Project participants should use Step 1 of the latest version of the Tool for the demonstration and assessment of additionality, to identify all realistic and credible baseline alternatives. In doing so, relevant policies and regulations related to the management of landfill sites should be taken into account. Such policies or regulations may include mandatory landfill gas capture or destruction requirements because of safety issues or local environmental regulations. Other policies could include local policies promoting productive use of landfill gas such as those for the production of renewable energy, or those that promote the processing of organic waste. In addition, the assessment of alternative scenarios should take into account local economic and technological circumstances. National and/or sectoral policies and circumstances must be taken into account in the following ways: In Sub-step 1b of the Tool for the demonstration and assessment of additionality, the project developer must show that the project activity is not the only alternative that is in compliance with all regulations (e.g. because it is required by law); Via the adjustment factor AF in the baseline emissions project participants must take into account that some of the methane generated in the baseline may be captured and destroyed to comply with regulations or contractual requirements; The project participants must monitor all relevant policies and circumstances at the beginning of each crediting period and adjust the baseline accordingly. Alternatives for the disposal/treatment of the waste in the absence of the project activity, i.e. the scenario relevant for estimating baseline methane emissions, to be analysed should include, inter alia: The project activity (i.e. capture of landfill gas and its flaring and/or its use) undertaken without being registered as a CDM project activity; Atmospheric release of the landfill gas or partial capture of landfill gas and destruction to comply with regulations or contractual requirements, or to address safety and odour concerns. If LFG is used for generation of electric or heat energy for export to a grid and/or to a nearby industry or used on-site, realistic and credible alternatives should also be separately determined for: Power generation in the absence of the project activity; Heat generation in the absence of the project activity. For power generation, the realistic and credible alternative(s) may include, inter alia: Power generated from landfill gas undertaken without being registered as CDM project activity; Existing or construction of a new on-site or off-site fossil fuel fired cogeneration plant; Existing or construction of a new on-site or off-site renewable based cogeneration plant; Existing or construction of a new on-site or off-site fossil fuel fired captive power plant; Existing or construction of a new on-site or off-site renewable based captive power plant; Existing and/or new grid-connected power plants. For heat generation, the realistic and credible alternative(s) may include, inter alia: Heat generated from landfill gas undertaken without being registered as CDM project activity; Existing or Construction of a new on-site or off-site fossil fuel fired cogeneration plant; Existing or Construction of a new on-site or off-site renewable based cogeneration plant; Existing or new construction of on-site or off-site fossil fuel based boilers, air heaters or other heat generating equipment (e.g. kilns); Existing or new construction of on-site or off-site renewable energy based boilers, air heaters or other heat generating equipment (e.g. kilns); Any other source such as district heat; and Other heat generation technologies (e.g. heat pumps or solar energy). Step 2: Identify the fuel for the baseline choice of energy source taking into account the national and/or sectoral policies as applicable Demonstrate that the identified baseline fuel is available in abundance in the host country and there is no supply constraint. In case of partial supply constraints (seasonal supply), the project participants may consider an alternative fuel that result in lowest baseline emissions during the period of partial supply. Detailed justification shall be provided for the selected baseline fuel. As a conservative approach, the lowest carbon intensive fuel such as natural gas through out the period may be used. Note: Steps 3 and 4 shall be applied for each component of the baseline, i.e. baseline for waste treatment, electricity generation and heat generation. Step 3: Step 2 and/or Step 3 of the latest approved version of the Tool for demonstration and assessment of additionality shall be used to assess which of these alternatives should be excluded from further consideration (e.g. alternatives facing prohibitive barriers or those clearly economically unattractive). Step 4: Where more than one credible and plausible alternative remains, project participants shall, as a conservative assumption, use the alternative baseline scenario that results in the lowest baseline emissions as the most likely baseline scenario. The least emission alternative will be identified for each component of the baseline scenario. In assessing these scenarios, any regulatory or contractual requirements should be taken into consideration. Note: The methodology is only applicable if: The most plausible baseline scenario for the landfill gas is identified as either the atmospheric release of landfill gas or landfill gas is partially captured and subsequently flared (LFG2); The most plausible baseline scenario for the energy component of the baseline scenario is one of the following scenarios described in Table 2 below. Table 2: Combinations of baseline options and scenarios applicable to this methodology ScenarioBaselineDescription of situationLandfill gasElectricityHeat1 LFG2 P4 or P6 H4 The atmospheric release of landfill gas or landfill gas is partially captured and subsequently flared. The electricity is obtained from an existing/new fossil based captive power plant or from the grid and heat from an existing/new fossil fuel based boiler, air heater or other heat generating equipment.As an alternative to the procedure given above the Combined tool to identify the baseline scenario and demonstrate additionality could be used. Same additional guidance as provided above should be used. Additionality The additionality of the project activity shall be demonstrated and assessed using the latest version of the Tool for the demonstration and assessment of additionality agreed by the CDM Executive Board, which is available on the UNFCCC CDM website. If the Combined tool to identify the baseline scenario and demonstrate additionality is used for the selection of the most plausible baseline scenario this same tool should be used for the demonstration of additionality. Baseline emissions  EMBED Equation.3  ( AUTONUMLGL \e ) Where: BEy=Baseline emissions in year y (tCO2e)MDproject,y =The amount of methane that would have been destroyed/combusted during the year, in tonnes of methane (tCH4) in project scenarioMDBL,y=The amount of methane that would have been destroyed/combusted during the year in the absence of the project due to regulatory and/or contractual requirement, in tonnes of methane (tCH4)GWPCH4 =Global Warming Potential value for methane for the first commitment period is 21tCO2e/tCH4ELLFG,y=Net quantity of electricity produced using LFG, which in the absence of the project activity would have been produced by power plants connected to the grid or by an on-site/off-site fossil fuel based captive power generation, during year y, in megawatt hours (MWh)CEFelecy,BL,y =CO2 emissions intensity of the baseline source of electricity displaced, in tCO2e/MWh This is estimated as per equation (9) belowETLFG,y=The quantity of thermal energy produced utilizing the landfill gas, which in the absence of the project activity would have been produced from onsite/offsite fossil fuel fired boiler/air heater, during the year y in TJCEFther,BL,y =CO2 emissions intensity of the fuel used by boiler/air heater to generate thermal energy which is displaced by LFG based thermal energy generation, in tCO2e/TJ. This is estimated as per equation (10) belowIn the case where the MDBL,y is given/defined in the regulation and/or contract as a quantity that quantity will be used. In situations where in the baseline LFG captured and destroyed, for reasons other than regulation and/or contract, historic data on actual amount captured shall be used as MDBL,y. In cases where regulatory or contractual requirements do not specify MDBL,y or no historic data exists for LFG captured and destroyed an Adjustment Factor (AF) shall be used and justified, taking into account the project context.  EMBED Equation.3  ( AUTONUMLGL \e ) Guidance on estimating AF: In cases where a specific system for collection and destruction of methane is mandated by regulatory or contractual requirements or is undertaken for other reasons, the ratio of the destruction efficiency of the baseline system to the destruction efficiency of the system used in the project activity shall be used. The following procedure should be followed: Step 1: Estimation of the destruction efficiency of the system In situations where the baseline specific system for collection and destruction of methane installed and operating prior to implementation of the project activity and measurements of the amount of methane that is destroyed are available then the following equation will be used:  EMBED Equation.3  ( AUTONUMLGL \e ) Where: BL=Destruction efficiency of the baseline system (fraction)MDHist=Amount of methane destroyed historically measured for the previous year before the start of project activity (tCH4)MGHist=Amount of methane generated historically for the previous year before the start of project activity, estimated using the actual amount of waste disposed in the landfill as per the latest version of the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal sitetCH4)While estimating ex ante methane emissions that are generated in the landfill with latest version of the approved Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal site the following guidance should be taken into account: In the tool, x will refer to the year since the landfill started receiving wastes [x runs from the first year of landfill operation (x=1) to the year for which emissions are calculated (x=y)]; Sampling to determine the different waste types is not necessary. The waste composition can be obtained from previous studies. In cases, where the baseline system for collection and destruction of methane is not installed prior to project implementation and/or measurements of the amount of methane that is destroyed are not available then the destruction efficiency of the system mandated by regulatory or contractual requirements (BL ) should be assumed to be equal to the theoretical efficiency of the specific system for collection and destruction of methane that is defined in the regulation or contract. In other cases, a procedure for estimating the amount of landfill gas that would be captured in absence of the project activity shall be provided in the CDM-PDD validated by the DOE. This procedure shall be used to estimate the MDHist in equation 3 above to estimate the baseline destruction efficiency; In cases where a specific percentage of the generated amount of methane to be collected and destroyed is specified in the contract or mandated by regulations, the efficiency of the baseline system ((BL) is equal to the defined specific percentage. Step 2: Estimation of the destruction efficiency of the system used in the project activity Option 1: The destruction efficiency of the system used in the project activity is estimated once and remains fixed for the whole crediting period and will be estimated as follows:  EMBED Equation.3  ( AUTONUMLGL \e ) Where: PR=Destruction efficiency of the system used in the project activity that will remain fixed for the whole crediting period (fraction)MDproject,1=Amount of methane destroyed by the project activity during the first year of the project activity (tCH4)MGPR,1=Amount of methane generated during the first year of the project activity estimated using the actual amount of waste disposed in the landfill as per the latest version of the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal site, see guidance in Step 1 (tCH4)Option 2: The destruction efficiency of the system used in the project activity is estimated every year as follows:  EMBED Equation.3  ( AUTONUMLGL \e ) Where: PR,y=Destruction efficiency of the system used in the project activity for year y (fraction)MDproject,y=Amount of methane destroyed by the project activity during the year y of the project activity (tCH4)MGPR,y=Amount of methane generated during year y of the project activity estimated using the actual amount of waste disposed in the landfill as per the latest version of the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal site, see further guidance in Step 1 (tCH4)Step 3: Estimation of the adjustment factor (AF) If Option 1 is used in Step 2 then:  EMBED Equation.3  ( AUTONUMLGL \e ) If Option 2 is used in Step 2 then:  EMBED Equation.3  ( AUTONUMLGL \e ) Where: AFy=Adjustment factor for year y, this factor will be used in equation 2 in place of AFProject proponents should provide an ex ante estimate of emissions reductions, by projecting the future GHG emissions of the landfill as specified below. MDproject,y will be determined ex post by metering the actual quantity of methane captured and destroyed once the project activity is operational. The methane destroyed by the project activity (MDproject,y) during a year is determined by monitoring the quantity of methane actually flared and gas used to generate electricity and/or produce thermal energy and/or supply to end users via natural gas distribution pipeline, if applicable, and the total quantity of methane captured. The sum of the quantities fed to the flare(s), to the power plant(s), to the boiler(s)/air heater(s)/heat generating equipment(s) and to the natural gas distribution network (estimated using equation 3) must be compared annually with the total quantity of methane generated. The lowest value of the two must be adopted as MD project,y. The following procedure applies when the total quantity of methane generated is the highest. The working hours of the energy plant(s) and the boiler(s)/air heater(s)/heat generating equipment(s) should be monitored and no emission reduction could be claimed for methane destruction in the energy plant or the boiler/air heater/heat generating equipment during non-operational hours.  EMBED Equation.3  ( AUTONUMLGL \e ) Where: MDflared,y=Quantity of methane destroyed by flaring (tCH4) MDelectricity,y=Quantity of methane destroyed by generation of electricity (tCH4) MDthermal,y=Quantity of methane destroyed for the generation of thermal energy (tCH4) MDPL,y =Quantity of methane sent to the pipeline for feeding to the natural gas distribution network (tCH4) Right hand side of the equation (3) is sum over all the points of captured methane use in case the methane is flared in more than one flare, and/or used in more than one electricity generation source, and/or more than one thermal energy generator. The supply to each point of methane destruction, through flaring or use for energy generation, shall be measured separately.  EMBED Equation.3  ( AUTONUMLGL \e ) Where: LFGflare,y =Quantity of landfill gas fed to the flare(s) during the year measured in cubic meters (m3)wCH4,y =Average methane fraction of the landfill gas as measured during the year and expressed as a fraction (in m CH4/m LFG)DCH4 =Methane density expressed in tonnes of methane per cubic meter of methane (tCH4/m3CH4) PEflare,y =Project emissions from flaring of the residual gas stream in year y (tCO2e) determined following the procedure described in the Tool to determine project emissions from flaring gases containing methane. If methane is flared through more than one flare, the PEflare,y shall be determined for each flare using the tool EMBED Equation.3  ( AUTONUMLGL \e ) Where: MDelectricity,y =Quantity of methane destroyed by generation of electricityLFGelectricity,y =Quantity of landfill gas fed into electricity generator EMBED Equation.3  ( AUTONUMLGL \e ) Where MDthermal,y is the quantity of methane destroyed for the generation of thermal energy and LFGthermal,y is the quantity of landfill gas fed into the boiler/air heater/heat generating equipment.  EMBED Equation.3  ( AUTONUMLGL \e ) Where LFGPL,y is the quantity of landfill gas sent to pipeline for feeding to the natural gas distribution network. Ex ante estimation of the the amount of methane that would have been destroyed/combusted during the year, in tonnes of methane (MDproject,y) The ex ante estimation of the the amount of methane that would have been destroyed/combusted during the year, in tonnes of methane (MDproject,y) will be done with the latest version of the approved Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal site, considering the following additional equation: MDproject,y = BECH4,SWDS,y/GWPCH4 ( AUTONUMLGL \e ) Where: BECH4,SWDS,y=Methane generation from the landfill in the absence of the project activity at year y (tCO2e), calculated as per the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal site. The tool estimates methane generation adjusted for, using adjustment factor (f) any landfill gas in the baseline that would have been captured and destroyed to comply with relevant regulations or contractual requirements, or to address safety and odor concerns. As this is already accounted for in equation 2, f in the tool shall be assigned a value 0 Furthermore the following guidance should be taken into account: In the tool x will refer to the year since the landfill started receiving wastes [x runs from the first year of landfill operation (x=1) to the year for which emissions are calculated (x=y)]; Sampling to determine the different waste types is not necessary, the waste composition can be obtained from previous studies. The efficiency of the degassing system which will be installed in the project activity should be taken into account while estimating the ex ante estimation. Determination of CEFelec,BL,y In case the baseline is electricity generated by an on-site/off-site fossil fuel fired captive power plant in the baseline, project proponents may use a default value of 0.8 tCO2/MWh or estimate the emission factor as follows:  EMBED Equation.3  ( AUTONUMLGL \e ) Where: EFfuel,BL =Emission factor of baseline fossil fuel used, as identified in the baseline scenario identification procedure, expressed in tCO2/mass of volume unitNCVfuel,BL=Net calorific value of fuel, as identified through the baseline identification procedure, in GJ per unit of volume or mass EMBED Equation.3 =Efficiency of baseline power generation plant3.6=Equivalent of GJ energy in a MWh of electricityTo estimate electricity generation efficiency, project participants may use the highest value among the following three values as a conservative approach: Measured efficiency prior to project implementation; Measured efficiency during monitoring; Data from manufacturer for efficiency at full load; Default efficiency of 60%. In case the baseline is electricity generated by plants connected to the grid the emission factor should be calculated according to Tool to calculate the emission factor for an electricity system. Determination of CEFther,BL,y  EMBED Equation.3  ( AUTONUMLGL \e ) Where: boiler/air heater =The energy efficiency of the boiler/air heater used in the absence of the project activity to generate the thermal energyNCVfuel,BL=Net calorific value of fuel, as identified through the baseline identification procedure, used in the boiler/air heater to generate the thermal energy in the absence of the project activity in TJ per unit of volume or massEFfuel,BL =Emission factor of the fuel, as identified through the baseline identification procedure, used in the boiler/air heater to generate the thermal energy in the absence of the project activity in tCO2 / unit of volume or mass of the fuel To estimate boiler efficiency, project participants may choose between the following two options: Option A Use the highest value among the following three values as a conservative approach: Measured efficiency prior to project implementation; Measured efficiency during monitoring; Manufacturers information on the boiler efficiency. Option B Assume a boiler efficiency of 100% based on the net calorific values as a conservative approach. To estimate air heater efficiency, assume an air heater efficiency of 100% based on the net calorific value of the fuel used as a conservative approach. In determining the CO2 emission factors (EFfuel) of fuels, reliable local or national data should be used if available. Where such data is not available, IPCC default emission factors should be chosen in a conservative manner.  EMBED Equation.3  ( AUTONUMLGL \e ) Where: PEEC,y=Emissions from consumption of electricity in the project case. The project emissions from electricity consumption (PEEC,y) will be calculated following the latest version of Tool to calculate baseline, project and/or leakage emissions from electricity consumption. If in the baseline a part of LFG was captured then the electricity quantity used in calculation is electricity used in project activity net of that consumed in the baselinePEFC,j,y =Emissions from consumption of heat in the project case. The project emissions from fossil fuel combustion (PEFC,j,y ) will be calculated following the latest version of Tool to calculate project or leakage CO2 emissions from fossil fuel combustion. For this purpose, the processes j in the tool corresponds to all fossil fuel combustion in the landfill, as well as any other on-site fuel combustion for the purposes of the project activity. If in the baseline part of a LFG was captured then the heat quantity used in calculation is fossil fuel used in project activity net of that consumed in the baseline.Leakage No leakage effects need to be accounted under this methodology. Emission Reduction Emission reductions are calculated as follows:  EMBED Equation.3  ( AUTONUMLGL \e ) Where: ERy=Emission reductions in year y (tCO2e/yr)BEy=Baseline emissions in year y (tCO2e/yr)PEy=Project emissions in year y (tCO2/yr)Data and parameters not monitored Data/Parameter:Regulatory requirements relating to landfill gasData unit:--Description:Regulatory requirements relating to landfill gasSource of data:Publicly available information of the host countrys regulatory requirements relating to landfill gasMeasurement procedures (if any):Any comment:The information though recorded annually, is used for changes to the adjustment factor (AF) or directly MDBL,y at renewal of the credit period. Relevant regulations for LFG project activities shall be updated at renewal of each credit period. Changes to regulation should be converted to the amount of methane that would have been destroyed/combusted during the year in the absence of the project activity (MDBL,y). Project participants should explain how regulations are translated into that amount of gas Date/Parameter:GWPCH4Data unit:tCO2e/tCH4Description:Global warming potential of CH4Source of data:IPCCMeasurement procedures (if any):21 for the first commitment period. Shall be updated according to any future COP/MOP decisionsAny comment: Data/Parameter:DCH4 Data unit:tCH4/m3CH4Description:Methane DensitySource of data:Measurement procedures (if any):At standard temperature and pressure (0 degree Celsius and 1,013 bar) the density of methane is 0.0007168 tCH4/m3CH4 Any comment: Data/Parameter:BECH4,SWDS,y Data unit:tCO2eDescription:Methane generation from the landfill in the absence of the project activity at year ySource of data:Calculated as per the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal siteMeasurement procedures (if any):As per the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal siteAny comment:Used for ex ante estimation of the amount of methane that would have been destroyed/combusted during the year Data/Parameter:MDHistData unit:tCH4Description:Amount of methane destroyed historically for the previous year before the start of project activity.Source of data:Project proponentMeasurement procedures (if any):Any comment:This parameter could be used for the estimation of AF Data/Parameter:MGHistData unit:tCH4Description:Amount of methane generated historically for the previous year before the start of project activitySource of data:Project proponentsMeasurement procedures (if any):Estimated using the actual amount of waste disposed in the landfill as per the latest version of the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal siteAny comment:This parameter could be used for the estimation of AFIII. MONITORING METHODOLOGY The monitoring methodology is based on direct measurement of the amount of landfill gas captured and destroyed at the flare platform(s), the natural gas pipelines and the electricity generating/thermal energy unit(s) to determine the quantities as shown in Figure 1. The monitoring plan provides for continuous measurement of the quantity and quality of LFG flared. The main variables that need to be determined are the quantity of methane actually captured MDproject,y, quantity of methane flared (MDflared,y), the quantity of methane used to generate electricity (MDelectricity,y)/thermal energy (MDthermal,y), the quantity of methane sent to the pipeline to the natural gas distribution network (MDPL,y) and the quantity of methane generated (MDtotal,y). The methodology also measures the energy generated by use of LFG (ELLFG,y, ETLFG,y) and energy consumed by the project activity that is produced using fossil fuels.  EMBED Word.Picture.8  Figure 1: Monitoring Plan To determine these variables, the following parameters have to be monitored: The amount of landfill gas generated (in m, using a continuous flow meter), where the total quantity (LFGtotal,y) as well as the quantities fed to the flare(s) (LFGflare,y), to the power plant(s) (LFGelectricity,y), sent to pipeline for feeding to the natural gas distribution network (LFGPL,y), and to the boiler(s)/air heater(s)/heat generating equipment(s) (LFGthermal,y) are measured continuously. In the case where LFG is just flared, one flow meter for each flare can be used provided that these meters used are calibrated periodically by an officially accredited entity; The fraction of methane in the landfill gas (wCH4,y) should be measured with a continuous analyzer; In all cases, methane fraction of the landfill gas and LFG flow have to be measured on same basis (either wet or dry). In case the Tool to determine project emissions from flaring gases containing methane is used, follow the standard approaches to convert the flow on wet basis to dry basis. For example, refer to the procedures provided in the book Fundamentals of Classical Thermodynamics; Gordon J. Van Wylen, Richard E. Sonntag and Claus Borgnakke; 4 Edition, 1994, John Wiley & Sons, Inc. The parameters used for determining the project emissions from flaring of the residual gas stream in year y (PEflare,y) should be monitored as per the Tool to determine project emissions from flaring gases containing methane; Temperature (T) and pressure (p) of the landfill gas are required to determine the density of methane in the landfill gas; The quantities of fossil fuels required to operate the landfill gas project, including the pumping equipment for the collection system and energy required to transport heat, should be monitored. In projects where LFG gas is captured in the baseline to either meet the regulation or for safety reason, fossil fuel used in the baseline too should be recorded; The quantity of electricity imported, in the baseline and the project situation, to meet the requirements of the project activity, if any; The quantity of electricity exported out of the project boundary, generated from landfill gas, if any; Relevant regulations for LFG project activities shall be monitored and updated at renewal of each credit period. Changes to regulation should be converted to the amount of methane that would have been destroyed/combusted during the year in the absence of the project activity (MDBL,y). Project participants should explain how regulations are translated into that amount of gas; The operating hours of the energy plant(s) and the boiler(s)/air heater(s)/heat generating equipment(s). The measurement equipment for gas quality (humidity, particulate, etc.) is sensitive, so a strong QA/QC procedure for the calibration of this equipment is needed. For this methodology, a continuous monitoring system for methane fraction of the landfill gas and LFG flow is one that continuously acquire data from the process (continuous sampling) in order to process it and deliver the required information (methane fraction of the landfill gas and LFG flow) as an average value in a time interval not greater than an hour. Paired values of the methane fraction of the landfill gas and LFG flow which are averaged for the same time interval should be used in the calculation of emission reductions (i.e. methane fraction of landfill gas averaged at hour x should be used with LFG flow which is averaged at the same hour x). Data and parameters monitored Data / Parameter:LFGtotal,yData unit:m3Description:Total amount of landfill gas captured at Normal Temperature and PressureSource of data:Project participantsMeasurement procedures (if any):Measured by a flow meter. Data to be aggregated monthly and yearlyMonitoring frequency:Continuous (average value in a time interval not greater than an hour shall be used in the calculations of emission reductions)QA/QC procedures:Flow meters should be subject to a regular maintenance and testing regime to ensure accuracyAny comment: Data / Parameter:LFGflare,yData unit:m3Description:Amount of landfill gas flared at Normal Temperature and PressureSource of data:Project participantsMeasurement procedures (if any):Measured by a flow meter. Data to be aggregated monthly and yearly for each flareMonitoring frequency:Continuous (average value in a time interval not greater than an hour shall be used in the calculations of emission reductions)QA/QC procedures:Flow meters should be subject to a regular maintenance and testing regime to ensure accuracyAny comment: Data / Parameter:LFGelectricity,yData unit:m3Description:Amount of landfill gas combusted in power plant at Normal Temperature and PressureSource of data:Project participantsMeasurement procedures (if any):Measured by a flow meter. Data to be aggregated monthly and yearly for each power plantMonitoring frequency:Continuous (average value in a time interval not greater than an hour shall be used in the calculations of emission reductions)QA/QC procedures:Flow meters should be subject to a regular maintenance and testing regime to ensure accuracyAny comment: Data / Parameter:LFGthermal,yData unit:m3Description:Amount of methane combusted in boiler/air heater/heat generating equipment at Normal Temperature and PressureSource of data:Project participantsMeasurement procedures (if any):Measured by a flow meter. Data to be aggregated monthly and yearly for each boiler/air heater/heat generating equipmentMonitoring frequency:Continuous (average value in a time interval not greater than an hour shall be used in the calculations of emission reductions)QA/QC procedures:Flow meters should be subject to a regular maintenance and testing regime to ensure accuracyAny comment: Data / Parameter:LFGPL,yData unit:m3Description:Amount of landfill gas sent to Pipe Line at Normal Temperature and PressureSource of data:Project participantsMeasurement procedures (if any):Measured by a flow meter. Data to be aggregated monthly and yearly for each flareMonitoring frequency:Continuous (average value in a time interval not greater than an hour shall be used in the calculations of emission reductions)QA/QC procedures:Flow meters should be subject to a regular maintenance and testing regime to ensure accuracyAny comment: Data / Parameter:PEflare,yData unit:tCO2eDescription:Project emissions from flaring of the residual gas stream in year ySource of data:Calculated as per the Tool to determine project emissions from flaring gases containing methaneMeasurement procedures (if any):As per the Tool to determine project emissions from flaring gases containing methaneMonitoring frequency:As per the Tool to determine project emissions from flaring gases containing methaneQA/QC procedures:As per the Tool to determine project emissions from flaring gases containing methaneAny comment:- Data / Parameter:wCH4Data unit:m CH4/m LFGDescription:Methane fraction in the landfill gasSource of data:To be measured continuously by project participants using certified equipmentMeasurement procedures (if any):Shall be measured using equipment that can directly measure methane content in the landfill gas, estimation of methane content of landfill gas based on measurement of other constituents of the landfill gas such as CO2 is not permitted. Measured by continuous gas quality analyserMonitoring frequency:Continuous (average value in a time interval not greater than an hour shall be used in the calculations of emission reductions)QA/QC procedures:The gas analyser should be subject to a regular maintenance and testing regime to ensure accuracyAny comment: Data / Parameter:TData unit:CDescription:Temperature of the landfill gasSource of data:Project participantsMeasurement procedures (if any):Measured to determine the density of methane DCH4. No separate monitoring of temperature is necessary when using flow meters that automatically measure temperature and pressure, expressing LFG volumes in normalized cubic metersMonitoring frequency:ContinuousQA/QC procedures:Measuring instruments should be subject to a regular maintenance and testing regime in accordance to appropriate national/international standardsAny comment: Data / Parameter:PData unit:PaDescription:Pressure of the landfill gasSource of data:Project participantsMeasurement procedures (if any):Measured to determine the density of methane DCH4. No separate monitoring of temperature is necessary when using flow meters that automatically measure temperature and pressure, expressing LFG volumes in normalized cubic metersMonitoring frequency:ContinuousQA/QC procedures:Measuring instruments should be subject to a regular maintenance and testing regime in accordance to appropriate national/international standardsAny comment: Data / Parameter:ELLFGData unit:MWhDescription:Net amount of electricity generated using LFGSource of data:Project participantsMeasurement procedures (if any):Electricity meterMonitoring frequency:ContinuousQA/QC procedures:Electricity meter will be subject to regular (in accordance with stipulation of the meter supplier) maintenance and testing to ensure accuracyAny comment:Required to estimate the emission reductions from electricity generation from LFG, if credits are claimed Data / Parameter:ETLFGData unit:TJDescription:Total amount of thermal energy generated using LFGSource of data:Project participantsMeasurement procedures (if any):-In case of steam meter: The enthalpy of steam and feed water will be determined at measured temperature and pressure and the enthalpy difference will be multiplied with quantity measured by steam meter. -In case of hot air: the temperature, pressure and mass flow rate will be measuredMonitoring frequency:ContinuousQA/QC procedures:In case of monitoring of steam, it will be calibrated for pressure and temperature of steam at regular intervals. The meter shall be subject to regular maintenance and testing to ensure accuracyAny comment:Required to estimate the emission reductions from thermal energy generation from LFG, if credits are claimed Data / Parameter:CEFelecy,BL,y Data unit:tCO2/MWhDescription:Carbon emission factor of electricitySource of data:Measurement procedures (if any):A default of 0.8 can be used if electricity in the baseline would have been produced using captive power plant. Else, equation 8 provides the estimation equation. In case the baseline source would have been grid, emission factor shall be estimated as described in Tool to calculate the emission factor for an electricity systemMonitoring frequency:AnnuallyQA/QC procedures:Any comment: Data / Parameter:EFfuel,BLData unit:tCO2/mass or volumeDescription:CO2 emission factor of fossil fuel.Source of data:The source of data should be the following, in order of preference: project specific data, country specific data or IPCC default values. As per guidance from the Board, IPCC default values should be used only when country or project specific data are not available or difficult to obtainMeasurement procedures (if any):Monitoring frequency:AnnuallyQA/QC procedures:Any comment:Fossil fuel that would have been used in the baseline captive power plant or thermal energy generation Data / Parameter:NCVfuel,BLData unit:GJ/mass or volume units of fuelDescription:Net calorific value of fossil fuelSource of data:The source of data should be the following, in order of preference: project specific data, country specific data or IPCC default values. As per guidance from the Board, IPCC default values should be used only when country or project specific data are not available or difficult to obtainMeasurement procedures (if any):Monitoring frequency:AnnuallyQA/QC procedures:Any comment:For fossil fuel that would have been used in the baseline for thermal energy generation and/or electricity generation Data / Parameter: EMBED Equation.3 Data unit:--Description:Efficiency of the baseline captive power plantSource of data:Measurement procedures (if any):To estimate electricity generation efficiency, project participants may use the highest value among the following three values as a conservative approach: Measured efficiency prior to project implementation; Measured efficiency during monitoring; Data from manufacturer for efficiency at full load; Default efficiency of 60%.Monitoring frequency:AnnuallyQA/QC procedures:Any comment: Data / Parameter: EMBED Equation.3 Data unit:--Description:Efficiency of the baseline boiler/air heater for producing thermal energy Source of data:Measurement procedures (if any):To estimate boiler efficiency, project participants may choose between the following two options: Option A Use the highest value among the following three values as a conservative approach: Measured efficiency prior to project implementation; Measured efficiency during monitoring; Manufacturers information on the boiler efficiency. Option B Assume a boiler efficiency of 100% based on the net calorific values as a conservative approach To estimate air heater efficiency, assume an air heater efficiency of 100% based on the net calorific value of fuel used as a conservative approachMonitoring frequency:AnnuallyQA/QC procedures:Any comment: Data / Parameter:Operation of the energy plantData unit:HoursDescription:Operation of the energy plantSource of data:Project participantsMeasurement procedures (if any):Monitoring frequency:AnnuallyQA/QC procedures:Any comment:This is monitored to ensure methane destruction is claimed for methane used in electricity plant when it is operational Data / Parameter:Operation of the boiler/air heater/heat generating equipment Data unit:HoursDescription:Operation of the boiler/air heater/heat generating equipment Source of data:Project participantsMeasurement procedures (if any):Monitoring frequency:AnnuallyQA/QC procedures:Any comment:This is monitored to ensure methane destruction is claimed for methane used in boiler/air heater/heat generating equipment when it is operational Data / Parameter:PEEC,y Data unit:tCO2Description:Project emissions from electricity consumption by the project activity during the year ySource of data:Calculated as per the Tool to calculate baseline, project and/or leakage emissions from electricity consumptionMeasurement procedures (if any):As per the Tool to calculate baseline, project and/or leakage emissions from electricity consumptionMonitoring frequency:As per the Tool to calculate baseline, project and/or leakage emissions from electricity consumptionQA/QC procedures:As per the Tool to calculate baseline, project and/or leakage emissions from electricity consumptionAny comment:- Data / Parameter:PEFC,j,y Data unit:tCO2eDescription:Project emissions from fossil fuel combustion in process j during the year ySource of data:Calculated as per the Tool to calculate project or leakage CO2 emissions from fossil fuel combustion.Measurement procedures (if any):As per the Tool to calculate project or leakage CO2 emissions from fossil fuel combustionMonitoring frequency:As per the Tool to calculate project or leakage CO2 emissions from fossil fuel combustionQA/QC procedures:As per the Tool to calculate project or leakage CO2 emissions from fossil fuel combustionAny comment:- Data / Parameter:MGPR,yData unit:tCH4Description:Amount of methane generated during year y of the project activity Source of data:Project proponentsMeasurement procedures (if any):Estimated using the actual amount of waste disposed in the landfill as per the latest version of the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal siteMonitoring frequency:AnnuallyQA/QC procedures:As per the latest version of the Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal siteAny comment:- IV. References and any other information Not applicable. - - - - - History of the document Version DateNature of revision11EB 47, Annex 6 28 May 2009Allow only the option of continuous measurement of methane content of the landfill gas; Include definition of continuous monitoring system.10EB 45, Annex 9 13 February 2009Include guidance for air heater efficiency; Include a clarification that emission reductions can be claimed for generation of thermal energy provided that the landfill gas displaces use of fossil fuel either in a boiler or in an air heater.09.1EB 43, Annex 2 24 October 2008Editorial changes to reflect that the source of data for the Regulatory requirements relating to landfill gas has been changed. Publicly available information should be used instead of contacting the DNA for collecting the information. 09EB 41, Annex 4 02 August 2008Following clarifications have been added: The measurement of both LFG flow and methane fraction in LFG have to be conducted on the same basis (wet or dry); Inclusion of cases where periodical measurements are allowed and guidance on performing periodical measurements for monitoring the fraction of methane in the landfill gas; The title of the Tool to determine methane emissions avoided from dumping waste at a solid waste disposal site changes to Tool to determine methane emissions avoided from disposal of waste at a solid waste disposal site.08.1EB 39, Paragraph 22 16 May 2008Tool to calculate baseline, project and/or leakage emissions from electricity consumption replaces the withdrawn Tool to calculate project emissions from electricity consumption. 08EB 36, Annex 10 30 November 2007 Clarify the procedure to calculate the Adjustment Factor, where in the baseline the landfill gas was captured and destroyed/used; Clarify how to apply the Tool to determine methane emissions avoided from the dumping waste at a solid waste disposal site for estimating ex-ante landfill gas emissions over the crediting period.07EB 35, Annex 11 19 October 2007 To include AM0002, AM0003, AM0010, and AM0011; Reference to the following tools was added: Tool to calculate project emissions from electricity consumption, Tool to calculate project or leakage CO2 emissions from fossil fuel combustion, and Combined tool to identify the baseline scenario and demonstrate additionality.06EB 32, Annex 6 22 June 2007 Include procedures for estimating emissions reductions from use of captured landfill gas for energy generation; Expand the applicability to project activities where the captured landfill gas is used to supply consumers through a natural gas distribution network. 05EB 28, Annex 9 15 December 2006 Replace the procedure for estimating flare efficiency with a reference to the Methodological Tool to determine project emissions from flaring gases containing methane.04EB 25, Annex 6 21 July 2006 Allow the use of one measurement point for LFG captured, if the captured LFG is flared only and not used for energy and/or electricity generation; Provide a default value for methane destruction flare efficiency (50%) should the methane destruction efficiency not be measured.03EB 24, Annex 6 12 May 2006 Reflect that separate monitoring of LFG temperature and pressure is not required if the monitoring equipment used automatically adjusts the volume for these two parameters; Incorporate the procedures of estimating emissions reductions to take into account situations where project activities may not utilize the captured LFG but require use of fossil fuel or purchased electricity in operating the project activity.02EB 21, Annex 9 30 September 2005 Guidance on how to estimate the Adjustment Factor (AF) was provided.01EB 15, Annex 1 03 September 2004 Initial adoption.  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The project developer must bear in mind the relevant clarifications on the treatment of national and/or sectoral policies and regulations in determining a baseline scenario as per Annex 3 to the Executive Board 22nd meeting and any other forthcoming guidance from the Board on this subject.  Please refer to: < HYPERLINK "http://cdm.unfccc.int/methodologies/PAmethodologies/approved.html"  HYPERLINK "http://cdm.unfccc.int/goto/MPappmeth" http://cdm.unfccc.int/goto/MPappmeth>.  Methane fraction of the landfill gas and LFG flow have to be measured on same basis (either wet or dry). In case the Tool to determine project emissions from flaring gases containing methane is used, follow the standard approaches to convert the flow on wet basis to dry basis. For example, refer to the procedures provided in the book Fundamentals of Classical Thermodynamics; Gordon J. Van Wylen, Richard E. Sonntag and Claus Borgnakke; 4 Edition, 1994, John Wiley & Sons, Inc.  At standard temperature and pressure (0 degree Celsius and 1,013 bar) the density of methane is 0.0007168 tCH4/m3CH4.     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