This protocolProtocol (A document that describes how to quantitatively assess the net amount of CO₂ removed by a process. To Isometric, a Protocol is specific to a Project Proponent's process and comprised of Modules representing the Carbon Fluxes involved in the CDR process. A Protocol measures the full carbon impact of a process against the Baseline of it not occurring.) provides the requirements and procedures for the calculation of net CO2e removal (The term used to represent the CO₂ taken out of the atmosphere as a result of a CDR process.) from the atmosphere via the conversion of biomass to bio-oil (A mixture of water, organic acids, aldehydes, ketones, sugars, phenols, and other organic compounds derived from the thermal breakdown of biomass. Thermal breakdown of biomass is achieved via thermochemical processes, such as pyrolysis, which heat biomass in low- or no-oxygen environments to high temperatures (~e.g. 350-650°C). Bio-oil is often also referred to as pyrolysis oil or bio-crude.) (and co-products) and injection of bio-oil into natural or engineered subsurface features or geologic formations which may include, but are not limited to, reservoirs, saline aquifers, caverns or mines, for long term sequestration of atmospheric CO2. Bio-oil Carbon Capture & Sequestration is considered a subsector of Biomass Carbon Removal and Storage (BiCRS) (A range of processes that use biogenic material to remove carbon dioxide (CO₂) from the atmosphere and store that CO₂ underground or in long-lived products (LLNL BiCRS Roadmap, 2020).). This protocolProtocol applies to bio-oil sequestration technologies or projects, which typically consist of activities (An activity or process or group of activities or processes that alter the condition of a Baseline and leads to Removals or Reductions.) associated with three sub-processes - biomass growth, biomass conversion, and bio-oil injection and storage.
Bio-oil is a mixture of water, organic acids, aldehydes, ketones, sugars, phenols, and other organic compounds derived from the thermal breakdown of biomass1. Thermal breakdown of biomass is achieved via thermochemical processes, such as pyrolysis, liquefaction, or gasification, which heat biomass in low- or no- oxygen environments to high temperature (approximately 350°-650°C). Bio-oil is often also referred to as pyrolysis oil or bio-crude.
Bio-oil can have co-products like biochar mixed into it ahead of injection underground. Within this Protocol, we use the words ‘bio-oil’, ‘bio-oil with biochar’ and ‘injectant’ interchangeably.
The protocolProtocol accounts for quantification of the gross amount of carbonCO2 removed via injection of bio-oil into geologic formations, as well as the accounting for all Greenhousegreenhouse Gasgas (GHG) emissions associated with the process, including growth, collection, use, and alternate usecollection of the biomass feedstock (Raw material which is used for CO₂ Removal or GHG Reduction.), biomass conversion, biomass injection process, and all transportation and embodied emissions (Life cycle GHG emissions associated with production of materials, transportation, and construction or other processes for goods or buildings.) associated with the process, and emissions associated with leakage (The increase in GHG emissions outside the geographic or temporal boundary of a project that results from that project's activities.). The GHG AssessmentStatement (TheA processdocument bysubmitted whichalongside allClaimed emissionsRemovals and/or Reductions that details the calculations associated with a Removal or Reduction, including the Project's emissions, Removals, Reductions and Leakages, presented together in net metric tonnes of CO₂e per Removal or Reduction process, including leakages, are accounted for.) is considered as a cradle-to-grave (Considering impacts at each stage of a product's life cycle, from the time natural resources are extracted from the ground and processed through each subsequent stage of manufacturing, transportation, product use, and ultimately, disposal.) analysis.
This protocolProtocol is developed to adhere to the requirements of ISO (A worldwide federation (NGO) of national standards bodies from more than 160 countries, one from each member country.) 14064-2: 2019 – Greenhouse Gases – Part 2: Specification with guidance at the project (An activity or process or group of activities or processes that alter the condition of a Baseline and leads to Removals or Reductions.) level for quantification, monitoring, and reporting of greenhouse gas (Those gaseous constituents of the atmosphere, both natural and anthropogenic (human-caused), that absorb and emit radiation at specific wavelengths within the spectrum of terrestrial radiation emitted by the Earth’s surface, by the atmosphere itself, and by clouds. This property causes the greenhouse effect, whereby heat is trapped in Earth’s atmosphere (CDR Primer, 2022).)emission reductions (Lowering future GHG releases from a specific entity.) or removal enhancements. The protocolProtocol ensures:
Specific Standards and protocols which are utilized as the foundation of this protocolProtocol and for which this protocolProtocol is intended to be fully compliant with are the following:
Additional reference standards that inform the requirements and overall practices incorporated in this protocolProtocol include:
Additional standards, methodologies, and protocols that were reviewed, referenced, or for which attempts to align with or leverage in development of this protocolProtocol include:
This protocolProtocol was developed based on the current state of the art and current publicly available science regarding biomass conversion and bio-oil injection. Because bio-oil injection and storage in geologic formations is a novel Carboncarbon Dioxidedioxide Removalremoval (CDR) approach, with limited published literature, the protocolProtocol incorporates requirements that may be more stringent than some current relevant regulations for underground injection, or other protocols related to biomass utilization for CDR.
This approach, notably when specifying requirements for demonstrating bio-oil storage (Describes the addition of carbon dioxide removed from the atmosphere to a reservoir, which serves as its ultimate destination. This is also referred to as “sequestration”.)durability (The amount of time carbon removed from the atmosphere by an intervention – for example, a CDR project – is expected to reside in a given Reservoir, taking into account both physical risks and socioeconomic constructs (such as contracts) to protect the Reservoir in question.) or permanence, will likely be altered in future versions of the protocolProtocol as the stability of bio-oil in geologic formations becomes well demonstrated and documented, reversal (The escape of CO₂ to the atmosphere after it has been stored, and after a Certificate has been Issued. A Reversal is classified as avoidable if a Project Proponent has influence or control over it and it likely could have been averted through application of reasonable risk mitigation measures. Any other Reversals will be classified as unavoidable.) risks are proven to be limited or non-existent, and the overall body of knowledge and data regarding all processes, from feedstock supply, to conversion, and to permanent storage is significantly increased.
This protocolProtocol applies to projects or processes which:
This protocolProtocol applies to projects and associated operations that meet all of the following project conditions:
Projects that are explicitly NOT eligible include the following:
The project must consider other environmental and social impacts and the projectProject proponentProponent (The organization that develops and/or has overall legal ownership or control of a Removal or Reduction Project.) must provide evidence that the project will do no net environmental or socioeconomic harm, complying with Section 3.7 of the Isometric Standard.
In addtionaddition to that outlined with the Isometric Standard, it must consider all aspects of the project from feedstock growth through injection and storage. At a minimum the projectProject proponentProponent must:
The following topics are covered briefly in this protocolProtocol due to their inclusion in the Isometric Standard, which governs all Isometric protocolsProtocols. See in-text references to the Isometric Standard for further guidance.
For each specific project to be evaluated under this protocolProtocol, the projectProject proponentProponent must document project characteristics in a Project Design Document (PDD) (The document that clearly outlines how a Project will generate rigorously quantifiable Additional high-quality Removals or Reductions.) as outlined in Section 3.2 of the Isometric Standard. The PDD will form the basis for project verification and evaluation in accordance with this protocolProtocol, and must include consideration of processes unique to bio-oil such as:
Projects must be validated (A systematic and independent process for evaluating the reasonableness of the assumptions, limitations and methods that support a Project and assessing whether the Project conforms to the criteria set forth in the Isometric Standard and the Protocol by which the Project is governed. Validation must be completed by an Isometric approved third-party (VVB).) and project net CO2e removals verified (A process for evaluating and confirming the net Removals and Reductions for a Project, using data and information collected from the Project and assessing conformity with the criteria set forth in the Isometric Standard and the Protocol by which it is governed. Verification must be completed by an Isometric approved third-party (VVB).) by an independent third party consistent with the requirements described in this Protocol as well as in Section 4 of the Isometric Standard.
The Validation and Verification Body (VVB) (Third-party auditing organizations that are experts in their sector and used to determine if a project conforms to the rules, regulations, and standards set out by a governing body. A VVB must be approved by Isometric prior to conducting validation and verification.) must consider following requisite components:
The threshold for Materiality (An acceptable difference between reported Removals/emissions or Reductions/emissions and what an auditor determines is the actual Removal/emissions or Reduction/emissions.), considering the totality of all omissions, errors and mis-statements, is 5%, in accordance with Section 4.3 of the Isometric Standard.
Verifiers should also verify the documentation of uncertainty (A lack of knowledge of the exact amount of CO₂ removed by a particular process, Uncertainty may be quantified using probability distributions, confidence intervals, or variance estimates.) of the GHG Statement (A document submitted alongside Claimed Removals and/or Reductions that details the calculations associated with a Removal or Reduction, including the Project's emissions, Removals, Reductions and Leakages, presented together in net metric tonnes of CO₂e per Removal or Reduction.) as required by Section 2.5.7 of the Isometric Standard. Qualitative materialityMateriality issues may also be identified and documented, such as5:
Project validation and verification must incorporate site visits to project facilities in accordance with the requirements of ISO 14064-3, 6.1.4.2, including, at a minimum, site visits during validation and initial verification to the biomass conversion site and the bio-oil injection site. Validators should, whenever possible, observe operation of the conversion and injection processes to ensure full documentation of process inputs and outputs through visual observation.
A site visit must occur at least once every 2 years at each location.
Verifiers and validators must comply with the requirements defined in Section 4 of the Isometric Standard. In addition, teams shall maintain and demonstrate expertise associated with the specific technologies of interest, including biomass growth, biomass conversion, bio-oil production and geologic storage.
Competency must be demonstrated through the below relevant sectoral scope accreditations listed below, orbased throughon demonstrationIAF ofMD relevant14 experience,and in accordance with Isometric's VVB policy:
CDR via bio-oil production and injection is often a result of a multi-step process (such as biomass growth, harvesting, transport, conversion, injection, and storage), with activities in each step managed and operated by a different operator, company, or owner. When there are multiple parties involved in the process (e.g., forestry owner or injection site operator), and to avoid double counting (Improperly allocating the same Removal or Reduction from a Project Proponent more than once to multiple Buyers.) of net CO2e removals, a single Project Proponent must be specified as the sole owner of the Credits. Contracts must comply with all requirements defined in Section 3.1 of the Isometric Standard.
The Project Proponent shall be able to demonstrate additionality through compliance with Section 2.5.3 of the Isometric Standard. The baseline (A set of data describing pre-intervention or control conditions to be used as a reference scenario for comparison.) scenario and counterfactual (An assessment of what would have happened in the absence of a particular intervention – i.e., assuming the Baseline scenario.) scenarios and baselines (A set of data describing pre-intervention or control conditions to be used as a reference scenario for comparison.) utilized to assess additionality must be project-specific, and are described inSection the7.2 Biomassof Feedstockthis Accounting 1.1.0 moduleProtocol.
Additionality determinations should be reviewed and completed every two years, at a minimum, or whenever project operating conditions change significantly, such as the following:
Any review and change in the determination of additionality shall not affect the availability of carbon finance and carbon credits (A publicly visible uniquely identifiable Credit Certificate Issued by a Registry that gives the owner of the Credit the right to account for one net metric tonne of Verified CO₂e Removal or Reduction. In the case of this Standard, the net tonne of CO₂e Removal or Reduction comes from a Project Validated against a Certified Protocol.) for the current or past creditingCrediting periodsPeriods (The period of time over which a Project Design Document is valid, and over which Removals or Reductions may be Verified, resulting in Issued Credits.), but, if the review indicates the project has become non-additional, this shall make the project ineligible for future credits6.
The uncertainty in the overall estimate of the net CO2e removal as a result of the project must be accounted for. The total net CO2e removed, CO2e([math: CO_2e_{Removal, n}]) for a specific batch ([math: n]) must be conservatively (Purposefully erring on the side of caution under conditions of Uncertainty by choosing input parameter values that will result in a lower net CO₂ Removal or GHG Reduction than if using the median input values. This is done to increase the likelihood that a given Removal or Reduction calculation is an underestimation rather than an overestimation.) determined based on the relevant requirements outlined in Section 2.5.7 of the Isometric Standard.
Projects must report a list of all input variables used in the net CO2e removal calculation and their uncertainties, including:
The uncertainty information should at least include the minimum and maximum values of aeach variable that goes into the net CO2e removal calculation. More detailed uncertainty information should be provided if available, as outlined in Section 2.5.7 of the Isometric Standard.
In addition, a sensitivity analysis (An analysis of how much different components in a Model contribute to the overall Uncertainty.) that demonstrates the impact of each input parameter’s uncertainty on the final net CO2e uncertainty must be provided. Details of the sensitivity analysis method must be provided such that a third party can reproduce the results. Input variables may be omitted from an uncertantyuncertainty analysis if they contribute to a < 1% change in the net CO2e removal. For all other parameters, information about uncertainty must be specified.
In accordance with the Isometric Standard, all evidence and data related to the underlying quantification of net CO₂e removal will be available to the public through Isometric's platform (A community resource where Project Proponents publish and visualize their early processes, Removal and Reduction data and Protocols – enabling the scientific community to share feedback and advice.). That includes:
The projectProject proponentProponent can request certain information to be restricted (only available to authorized buyersBuyers (An entity that purchases Removals or Reductions, often with the purpose of Retiring Credits to make a Removal or Reduction claim.), the Registry (A database that holds information on Verified Removals and Reductions, and reviewed EACs, based on Protocols. Registries Issue Certificates, and track their ownership and Retirement.) and VVB) where it is subject to confidentiality. This includes emissions factors from licensed databases. However, thatall does not apply to anyother numerical data produced or used as part of the quantification of net CO2e removal will be made available.
The scope of this protocolProtocol includes GHG sources, sinks (Any process, activity, or mechanism that removes a greenhouse gas, a precursor to a greenhouse gas, or an aerosol from the atmosphere.), and reservoirs (SSRs) associated with a bio-oil injection CDR project. A cradle-to-grave GHG Statement must be prepared encompassing the GHG emissions relating to SSRs controlled by and related to the project, including the following activities:
It should be noted that the physical and system boundaries for the bio-oil injection and storage site should include the following subprocess:
Emissions for processes within the system boundary shall include all GHG SSRs from the construction or manufacturing of each physical site and associated equipment, closure and disposal of each site and associated equipment, and operation of each process (biomass production, biomass conversion, bio-oil injection), to include embodied emissions of equipment and consumables in the process. Any emissions required to source the feedstock must be accounted for. These include feedstock collection/harvest, preparation, and transportation. The Project Proponent is responsible for identifying all sourcesGHG of emissionsSSRs directly or indirectly related to project activities.
Any emissions from sub-processes or process changes that would not have taken place without the involvement of the CDR process, such as subsequent transportation and refining, must be fully considered in the system boundary. This allows for accurate consideration of additional, incremental emissions induced by the CDR process.
Note that this protocol does not require inclusion of emissions resulting from ancillaryAncillary activities not directly related to project operations, (such as supplementary research and development activities, and corporate administrative activities) andthat anyare associated facilitieswith a project but are not directly or indirectly related to the issuance of Credits can be excluded from the system boundary.
In addition, biomass conversion pyrolysis processes will typically produce co-products of biochar and ash, withand potentialpotentially other products. This protocol does not account for the production and use of those co-products and assigns allAll emissions associated with the entire system where bio-oil and co-products are produced must be allocated to the bio-oilCDR that is injected as a conservative estimateprocess.
When biochar is mixed into the bio-oil ahead of the injection, anyemissions emittingassociated with all activities or materials related to thatbiochar processproduction must be accounted for in totality.
Carbon fluxes (The amountsystem ofboundary carbonfor exchangedGHG betweenaccounting twomust orinclude moreall ReservoirsSSRs overcontrolled a period of time.)by and associatedrelated GHG emissions (positive and negative (Occur when a Sink – created or enhanced by human activity – removes greenhouse gasses from the atmosphere (CDR Primer, 2022).)) fromto the project may derive from, including but are not limited to, the following sourcesSSRs in Table 1:.
Table 1. Scope of activities and GHG SSRs to be included by the removal project
| Emission Category | GHG source, sink or reservoir | GHG | Included? | Justification | |||||
|---|---|---|---|---|---|---|---|---|---|
| Fuel Use (harvesting and/or collection) | CO2 | Yes | Primary emission from fuel combustion | |||||
CH4 | Yes | Potential release during fuel combustion; included for completeness | |||||||
N2O | Yes | ||||||||
| Electricity Use (harvesting and/or collection) | CO2 | Yes | Primary emission from electricity generation | ||||||
CH4 | Yes | Potential release during electricity generation; included for completeness | |||||||
N2O | Yes | ||||||||
CO2 | Yes |
| |||||||
CH4 | Yes | CH4 release possible depending on manufacturing process and energy consumption | |||||||
N2O | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
| Land Use Change | CO2 | Yes | Accounting framework outlined in the Biomass Feedstock Accounting 1. | ||||||
CH4 | Yes | ||||||||
N2O | Yes | ||||||||
Biomass Processing | Electricity Use | CO2 | Yes | Primary emission from electricity generation | |||||
CH4 | Yes | Potential release during electricity generation; included for completeness | |||||||
N2O | Yes | ||||||||
| Process Emissions | CO2 | Yes | Release possible depending on processing method, e.g. tail gases released during pyroylsis | ||||||
CH4 | Yes | ||||||||
N2O | Yes | Release possible depending on processing method. May be demonstrated as negligible and excluded | |||||||
Embodied emissions – equipment manufacture, construction, demolition | CO2 | Yes | Primary emission from manufacture of equipment due to energy consumption | ||||||
CH4 | Yes | CH4 release possible depending on manufacturing process and energy consumption | |||||||
N2O | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
| Embodied emissions - other consumables | CO2 | Yes | Primary emission from manufacture of consumables due to energy consumption | ||||||
CH4 | Yes | CH4 release possible depending on manufacturing process and energy consumption | |||||||
N2O | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
Bio-oil Injection | Electricity Use | CO2 | Yes | Primary emission from electricity generation | |||||
CH4 | Yes | Potential release during electricity generation; included for completeness | |||||||
N2O | Yes | ||||||||
| Process Emissions | CO2 | Yes | Emissions from the process (aside from energy use) are not anticipated, since bio-oil will be injected directly. Venting of the storage might be required | ||||||
CH4 | Yes | ||||||||
N2O | Yes | ||||||||
Embodied emissions – equipment manufacture, construction, demolition | CO2 | Yes | Primary emission from manufacture of equipment due to energy consumption | ||||||
CH4 | Yes | CH4 release possible depending on manufacturing process and energy consumption | |||||||
N2O | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
| Embodied emissions - other consumables | CO2 | Yes | Primary emission from manufacture of consumables due to energy consumption | ||||||
CH4 | Yes | CH4 release possible depending on manufacturing process and energy consumption | |||||||
N2O | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
| Carbon in injected Bio-oil | CO2 | Yes | |||||||
Transportation between Biomass Production, Conversion, & Injection | Fuel Use | CO2 | Yes | Primary emission from biomass and bio-oil transport | |||||
CH4 | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
N2O | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
Embodied emissions – transportation equipment manufacture, construction, demolition | CO2 | Yes | Primary emission from manufacture of equipment due to energy consumption | ||||||
CH4 | Yes | CH4 release possible depending on manufacturing process and energy consumption | |||||||
N2O | Yes | Included for completeness. May be demonstrated as negligible and excluded | |||||||
Bio-oil | GHG emissions from storage formation | CO2 | Yes | Should not occur if properly designed and maintained. Included for completeness | |||||
CH4 | Yes | Should not occur if properly designed and maintained. CH4 may be generated by bio-oil decay. Included for completeness | |||||||
N2O | No | Not likely to occur in subsurface environment |
The Project Proponent must consider all GHGs associated with SSRs, in alignment with the United States Environmental Protection Agency’s definition of GHGs.All GHGs must be quantified and converted to CO2eCO2e in the GHG Statement using the 100-yr Global Warming Potential (GWP) for the GHG of interest, based on the most recent volume of the IPCC Assessment Report (currently the Sixth Assessment Report).
The projectbaseline proponentscenario shallfor usebio-oil projects assumes the frameworkactivities providedassociated in Section 2.5.2 ofwith the Isometric Standard as well as in this protocol to establish their GHG baseline. Development of a GHG baseline allows consistent comparison of abio-oil project activities’do effectsnot totake place and any existinginfrastructure oris alternativenot projects,built.
The activities,counterfactual oris technologiesthe thatCO2 would be consideredstored in the absencebiomass of a proposed project.
The GHG baseline must be developed for the specific project and consider specific alternative uses of biomassfeedstock that would have occurredremained durably stored in the biomass in the absence of the project. TheThis GHGis baselineknown mustas alsoineligible considerbiomass, given that the baselineCO2 relativestored would have remained stored in the biomass in the absence of the CDR project and is therefore not eligible to eachcount feedstocktowards used,Crediting. ifThe Biomass Feedstock Accounting Module 1.2 sets out requirements for establishing ineligible biomass as part of the projectCounterfactual utilizesStorage multipleEligibility feedstockcriteria. typesThe Biomass Feedstock Accounting Module 1.2 includes details for quantification of [math: CO_2e_{Counterfactual}].
The biomass pyrolysis process can be modeled as operating on a batch basis, consisting of a ‘Production Batch’, [math: p], which typically consists of utilizing a single type of biomass feedstock, often of a single source of origin, converting the biomass to bio-oil via pyrolysis, and storing and transporting that bio-oil to an injection site. The unique characteristics of the biomass used, its baseline or counterfactual, the bio-oil conversion process, the produced bio-oil characteristics, transportation distances, and storage site characteristics will be consistent for each Production Batch.
An ‘Injection Batch’, [math: n], is a single injection activity where a quantity of bio-oil is injected into an approved underground storage site. The Injection Batch may consist of a portion of a Production Batch, a full single Production Batch, or a blend of multiple Production Batches, which is injected for durable storage.
The approach for emissions calculations here is based on Injection- Batches and the specific calculation of net CO2e removal for each Injection Batch. The following sections outline the process for calculating the net CO2e removed for each specific Injection Batch batch of biomass processed and associated bio-oil injection, defined as a Removal.
WhenThe Reporting Period for a bio-oil project represents an interval of time over which removals are calculated and reported for verification. When total net CO2e removalremovals must be calculated for anya specifiedReporting reportingPeriod, periodfor example during submission of Claimed Removals in a GHG statement, it is calculated as the sum of the net CO2e removal of all Injection Batchesremovals during the reportingReporting periodPeriod:
[math: CO_2e_{Removal,\ RP} =\sum_{1}^{n}\ CO_2e_{Removal,\ n}]
(Equation 1)
Where
TotalNote: emissionsReversals reductionsoccur mayafter beCredits adjustedhave been issued so are not included in futurethis yearsequation. for a reporting period, [math: RP], due to reversals (see Storage Modules inSee Section 8) that may occur over the duration5.6 of the long-termIsometric storageStandard periodfor further information.
Net CO2e removal for a process utilizing biomass conversion to bio-oil and bio-oil injection into geologic formationproject can be calculated as follows. Note that the calculation is completed for a discrete batch, [math: n], of bio-oil that is injected (‘Injection Batch’). The final net CO2e quantification must be conservatively determined, giving high confidence that at least the estimated amount of carbonCO2e was removed.
[math: CO_2e_{Removal,\ n} = CO_2e_{Stored,\ n}\ –\ CO_2e_{Counterfactual,\ n}\ - \\ CO_2e_{LCA\Emissions,\ n}]
(Equation 2)
Where
[math: CO_2e_{Stored}] represents the amount of carbon as CO2e contained(stored inas theorganic injectantcarbon, C) that is injected and stored in the geologic or engineered storage formation. This is the gross amount stored for each batch injection and does not account for spillage nor reversals of storage from the storage formation.
The total amount of carbon dioxide equivalentCO2 contained in the injectant thatcan is injected into a geologic formation is considered the gross amount of CO2e stored, or [math: CO_2e_{Stored}],be calculated as: follows.
Where all bio-oil production batches are blended prior to injection:
[math: CO_2e_{Stored,\ n} = \frac{C_{Bio-oil,\ n}\cdot m_{Inj,\ n}}{C_{CO_{2}}}]
(Equation 3)
Where bio-oil production batches are not blended prior to injection:
[math: CO_2e_{Stored,\ n} = \sum_{p=1}^{k} \bigg(\frac{C_{Bio-oil,\ p}\cdot m_{Inj,\ p}}{C_{CO_{2}}} \bigg)]
(Equation 4)
Where:
Calculation of [math: CO_2e_{Stored}] requires two primary measurements:
TheIn valueorder ofto determine [math: C_{Bio -oil}], the %wt of C in the bio-oil injectant for either a blended bio-oil in Injection Batch [math: n], or for individual Production Batches [math: p], is determined via the analysis of samples of bio-oil injectant for total carbonC content.
The Acceptablefollowing test methodsmethod should be used where possible, and must be used for totalbio-oils carbonor contentblends includewith vapor pressures higher than 3 psi7:
Where this is not possible, other acceptable test methods include:
A minimum of one sample per Injection Batch (for blended injections) or one per Production Batch (for non-blended injections) of bio-oil must be collected and analyzed. Samples shall be from a well mixed and representative aliquot of the bio-oil as injected, insuring that solids are blended in the sample and representative of the amount in the injectant.
Analysis must be completed by a qualified laboratory, as evidenced by accreditation to ISO 17025 or equivalent standards (Standard physical constants as well as standard values set forth by bodies such as the National Institute of Standards and Technology (NIST) or others.) for laboratory quality management for the specific test method (ASTM D5291).
Laboratories shall complete standard quality assurance procedures on a schedule in accordance with their quality management plans and accreditation requirements to include:
This protocolProtocol provides two alternative methods for how often carbonC content must be measured and quantified. The first method (A) involves measuring every batch, the second method (B) involves only sampling some batches, and conservatively estimating the carbonC content of unsampled batches.
Method A: Measure every Batch
UsingThe this method, the carbonC content of every Injection Batch must be ascertained through direct measurement, either by:
For the acceptable minimum number of samples to take per sampled Batch, see Minimum number of samples per Batch below. If multiple samples are taken per Batch, the average carbonC content of these samples must be used.
Method B: Sampling a Production Process
For a given Production Process of a feedstock, samples must be taken directly for at least 30 Production Batches, to ensure there is enough data to estimate carbonC content for future Production Batches with appropriate statistical significance. Until this threshold is reached, Method A must be used.
Subsequently, samples must be taken at least every 10 Production Batches.
For the acceptable minimum number of samples to take per Batch, see Minimum number of samples per Batch below.
For batches which are not sampled, carbonC content must be conservatively estimated, as follows:
[math: C_{Bio-oil} = \mu_{CC} - \sigma_{\overline{CC}}]
(Equation 5)
[math: \sigma_{\overline{CC}} = \frac{\sigma_{CC}}{\sqrt{n_{samples}}}]
(Equation 6)
where:
Eligible samples are those taken in the previous 6 months before a specific Production Batch was produced. Older samples may not be used.
Additionally, batches must be subject to random sampling, to alleviate the risk of any given batch containing a substance with a substantially different carbonC content.
A random sampling approach must be agreed and documented in the Project Design Document, whereby Isometric will contact the Project Proponent on randomly selected days, at an agreed cadence, which must be no less frequent than once per month, on average. Once contacted, the Project Proponent must sample the carbonC content of the subsequent batches processed.
If the Project Proponent is unable to carry this random sampling out on 3 occasions within a 6 month period, or within a 6 month period more than 3 measurements are below 3 SD from the mean, this will trigger a Project review by Isometric.
If there is a significant change to a Production Process for a feedstock, which is likely to alter the average carbonC content of the feedstock, or if significant deviations in carbon content are detected, the feedstock should be considered as a new Production Process. This means that sampling must be restarted, with all prior samples no longer able to be used for estimating carbonC content.
Minimum number of samples per Batch
For all measurements taken, samples must be from a well mixed and representative aliquot of the injectant. To account for the possibility of variation within a single Production Batch (for example within a large container of the injectant), either of the following approaches must be adopted:
Process for handling carbonC content measurement outliers
For a given Production Process, an Outlier is defined as any individual sample which lies more than 3 standard deviations, [math: \sigma_{CC}], above or below the mean. To minimize the potential overall impact of outlier measurements, all carbonC content measurement outliers must be handled via the applying the technique of "winsorization”, as follows.
For a given measurement, [math: m], the winsorized measurement [math: m_w] is defined as follows:
The winsorized measurement, [math: m_w], must be used for the determination of carbon content.
This winsorization process must only be applied once a minimum number of 30 measurements have been taken, to ensure statistical significance.
The Project Proponent must monitor occurrences of outliers, and investigate if significantly more than the statistically expected number occurs, as it may be indicative of a systematic issue. This may be checked at verification, at the discretion of the verifying VVB.
The mass of injectant, [math: m_{Inj}], is measured via determination of weight of delivered bio-oil to the injection site using a calibrated scale. The total mass injected may be determined by the difference in bio-oil delivery truck weight measured upon arrival at the injection facility and at departure, after offloading of bio-oil, either into storage or directly to injection.
Any truck scale used must have a current certification (The Isometric process which involves expert review and Public Consultation in order to arrive at an approved version of a Protocol, against which Projects will be Validated and Removals or Reductions will be Verified.) in accordance with applicable local, state, or federal regulations for legal-for-trade weights and measures. Testing and calibration of scales must utilize certified weights in accordance with local, state, or other regulations, calibration weights must meet NIST Handbook 44 specifications9, and scale testing and calibration must be performed by a state certified entity.
The total mass injected may also be determined by other methods, such as use of a calibrated flow meter and density measurement, or use of calibrated on site weigh scales for smaller containers, where such methods are viable and justified. Note that, due to typical viscosity of bio-oil, the use of flow meters is not often viable and can result in poor data quality.
The projectProject proponentProponent must maintain the following records as evidence of gross CO2e storedremoval in injected bio-oil:
Records of all C analyses and injection masses (e.g. weigh scale tickets) must be maintained by the injection facility and provided for verification purposes for a period of five years.
Although limited and of small quantity, injection processes should be monitored to ensure that any process upsets or equipment failures and resulting spills of bio-oil are monitored, documented, quantified, and accounted for in the lifeGHG cycleStatement analysis(A document submitted alongside Claimed Removals and/or Reductions that details the calculations associated with a Removal or Reduction, including the Project's emissions, Removals, Reductions and Leakages, presented together in net metric tonnes of CO₂e per Removal or Reduction.) of the project batch. For each batch, where a process upset results in loss of bio-oil, that amount must be deducted from the delivered amount of bio-oil based on delivery weigh tickets. Such amounts must be allocated directly to the specific injection batch of bio-oil.
The calculation of [math: CO_2e_{Counterfactual,\ n}], equivalent to [math: CO_2e_{Feedstock}], is determined by the requirements of the Biomass Feedstock Accounting Module.
See Section 3 of the Biomass Feedstock Accounting Module
[math: CO_2e_{GHG\ Emissions,\ n}] is the total quantity of GHG emissions from operations and allocated embodied emissions for a batch [math: n]. This can be calculated as:
[math: CO_{2}e_{GHGEmissions,\ n} = CO_{2}e_{Energy,\ n} + CO_{2}e_{Transportation,\ n} \\ + CO_{2}e_{Embodied,\ n} +CO_2e_CO_{Monitoring2}e_{Misc.,\ n} \\ + CO_{2}e_{Misc. ProjectLeakage, n}]
(Equation 7)
Where
Note: Reversals occur after Credits have been issued so are not included in this equation. See Section 5.6 of the Isometric Standard for further information. Risk of reversal information is provided within the relevant Storage Module.
Emissions that occur relating to a batch, [math: n], must be included in the reporting of emissions associated with that batch and may not be allocated across multiple batches. Allocation across multiple batches must be agreed with Isometric on a case by case basis.
Embodied emissions which relate to multiple batches may be allocated in line with the allocation rules set out in the Embodied Emissions Accounting Module.
When the Project Proponent is planning to cease operations within a given storage site, the monitoring emissions required for post-closure monitoring must be calculated and allocated to the remaining removals taking place at the storage site. If that is not possible, the Project Proponent should allocate those emissions to other projects and/or storage sites they conduct removal operations at, in agreement with Isometric. If for any reason emissions are not appropriately allocated, the Reversal process will be triggered in accordance with Isometric Standard, to account for any remaining monitoring emissions.
In instances where monitoring activities are shared between entities, for example if multiple companies inject bio-oil into the same storage infrastructure, the emissions associated with these activities must be allocated proportionally between the entities.
EmissionsGHG emissions associated with energy[math: CO_2e_{Energy, n}] should include all emissions associated with electricity usage, through electricity or fuel combustion.
Examples of electricity usage may include, but are not limited to:
Examples of fuel consumption may include, but are not limited to:
The Energy Use Accounting Module provides guidance on how energy-related emissions must be calculated so that they can be subtracted in the net CO2e removal calculation. It sets out the calculation approach to be followed for intensive facilities and non-intensive facilities and acceptable emissions factors.
Refer to Energy Use Accounting Module for the calculation guidelines.
Emissions related to transportation of products as part of a batch [math: n]’s process.
Refer to Transportation Emissions Accounting Module for the calculation guidelines.
GHG emissions associated with [math: CO_2e_{Transportation, n}] should include all emissions associated with transportation of products as part of a batch [math: n]’s process, including the following:
Refer to Transportation Emissions Accounting Module for the calculation guidelines.
ExamplesThe Project Proponent must identify all equipment and consumables used in the biomass conversion and storage process, identify appropriate cradle to grave emission factors, and allocate the emissions to removals appropriately in line with the Embodied Emissions Accounting Module.
GHG emissions associated with [math: CO_2e_{Embodied, n}] should include all emissions associated with the procurement and use of materials, consumables and equipment, that must be considered as part of the embodied emission calculation includeincluding but are not limited to:
Refer to Embodied Emissions Accounting Module for the calculation guidelines.
Miscellaneous GHG emissions forassociated a batchwith [math: CO_2e_{Misc., n}], should include all emissions associated with the project that cannot be categorized by [math: CO_2e_{Energy,\ n}], [math: CO_2e_{Transport,\ n}], or [math: CO_2e_{Embodied\ n}]. The Project Proponent is responsible for identifying all sources of emissions directly or indirectly related to project activities and must report any outside of the SSR categories identified as miscellaneous emissions.
Examples include, but are not limited to:
Calculation of CO2eTailgas, n
Direct emissions from a pyrolysis process may occur when pyrolysis gasses are emitted to the atmosphere, are combusted within the process or pyrolyzer to provide thermal energy for the process, or are combusted or oxidized in an emissions control process such as a flare or thermal oxidizer.
Emissions are calculated as follows:
[math: CO_2e_{Tailgas,\ p}\ =\\ m_{Tailgas} \cdot C_{Tailgas,\ CH_4}\ \cdot GWP_{CH_4}\ \cdot t_p]
(Equation 8)
Where:
Measurement - CO2eTailgas, n
Quantification of [math: CO_2e_{Tailgas}] requires two primary measurements, the measurement of tail gas flow and the analysis of gas for CH4 content. CO2 content is not included as part of the [math: CO_2e_{Tailgas}] emissions as the Biomass Accounting Module requires that only biomass which would have decayed within 15 years is used. Therefore the immediate emissions of CO2 due to pyrolysis are not discounted against the totalnet CO2e removal due to the similarity of time horizons between these emissions and the counterfactual storage.
Tail gas flow rate, [math: m_{Tailgas}] can be determined by various acceptable methods, including:
The concentration of CH4 in the tail gas must be measured directly via one of the following methods:
Required Records & Documentation - CO2eTailgas, n
The projectProject proponentProponent must maintain the following records as evidence supporting calculation of emissions from the biomass conversion process:
[math: CO_2e_{Leakage,\ n}] includes emissions associated with a project's impact on activities outside the system boundary of the project. This includes instances where the Project causes an increase in GHG emissions by diverting material from other uses or incentivizing increased production activity.
It is the Project Proponent's responsibility to identify potential sources of leakage emissions. For a bio-oil project, replacement emissions (Any emissions that occur to compensate for biomass that was previously serving another purpose and is now being used for carbon removal or GHG reduction. For example, if agricultural waste was previously left on a field to decompose - fertilizer production to replace those nutrients need to be accounted for.) must be considered as a minimum. calculations required for replacement emissions associated with market leakage are set out in the Biomass Feedstock Accounting Module.
In line with the Eligibility Criteria set out in the Biomass Feedstock Accounting Module, projects which would lead to ecological leakage associated with land use change are not eligible under this Protocol.
See Section 3 of the Biomass Feedstock Accounting Module
This Protocol provides two options for durable storage of bio-oil. The Project Proponent can choose from available options when submitting their Project for verification.
Durability and monitoring requirements for storage in permeable reservoirs.
Durability and monitoring requirements for storage in salt caverns.
Isometric would like to thank following contributors to this Protocol and relevant modulesModules:
Isometric would like to thank following reviewers of this Protocol and relevant modules:
This appendix details how the Project Proponent must monitor, document and report all metrics
identified within this Protocol. Following this guidance will ensure the Project Proponent measures
and confirms carbon removeddioxide removal and long-term storage compliance, and will enable quantification of the
emissions removal resulting from the Project activity during the Project Crediting Period, prior to each Verification.
This methodology utilizes a comprehensive monitoring and documentation framework that captures the GHG impact in each stage of a Project. Monitoring and detailed accounting practices must be conducted throughout to ensure the continuous integrity of the carbon removals and crediting.
The Project Proponent must develop and apply a monitoring plan according to ISO 14064-2 principles of transparency and accuracy that allows the quantification and proof of GHG emissions removals.
The Modules associated with this Protocol have their own set of required parameters that need to be monitored. Please refer to the following Sections of the Modules to see a complete list of all requirements:
These parameters must be monitored for the purpose of Carbon Emissions Calculation and Embodied Carbon Emissions Calculation.
| Parameter | Parameter Description | Required | Equation | Parameter Type | Units | Data Source | Measurement Method | Monitoring Frequency | QA/QC Procedures | Required Evidence | Reference |
|---|---|---|---|---|---|---|---|---|---|---|---|
| [math: C_{Bio-oil,\ n}] | %wt of C in the bio-oil injectant | Always | Eq. 4 (Bio-oil Geological Storage) | Measured | wt% | Analytical determination of carbon content of bio-oil | ASTM D5271, ASTM D5373, NREL or similar / equivalent method for carbon content analysis | Measure per injection/production batch, or if 30 samples with the same feedstock type & processing have been taken within a 6 month period, this may be changed to a minimum of every 10 production batches, as well as random sampling. Minimum number of 3 samples per Batch measured, unless minimal ‘within batch’ variation can be justified. See ‘Biomass Carbon Content Measurement’ section for full details | ISO 17025 accredited laboratory | Analytical reports from qualified laboratory for audited samples, including supporting lab QA/QC results | 7.4.1 (Bio-oil Geological Storage) |
| [math: m_{Inj,\ n}] | Total mass of bio-oil injectant | Always | Eq. 4 (Bio-oil Geological Storage) | Measured | kg | Direct mass measurement | Calibrated Weigh Scale | Each bio-oil delivery | Scales must be calibrated annually by certified entity | Weigh scale tickets for each delivery of bio-oil (arrival and departure weights) or equivalent; Calibration records for scales | 7.4.1 (Bio-oil Geological Storage) |
| [math: C_{Bio-oil,\ p}] | %wt of C in the bio-oil injectant | Under certain conditions:
| Eq. 4 (Bio-oil Geological Storage) | Measured | wt% | Analytical determination of carbon content of bio-oil | ASTM D5291, NREL Laboratory Analysis Procedure for Determination of Carbon, Hydrogen, and Nitrogen in Bio-oils, or equivalent | One sample per production batch | ISO 17025 accredited laboratory | Analytical reports from qualified laboratory for audited samples, including supporting lab QA/QC results | 7.4.1 (Bio-oil Geological Storage) |
| [math: m_{Inj,\ p}] | Total mass of bio-oil injectant | Under certain conditions:
| Eq. 4 (Bio-oil Geological Storage) | Measured | kg | Direct mass measurement | Calibrated Weigh Scale | Each Bio-oil delivery | Scales must be calibrated annually by certified entity | Weigh scale tickets for each delivery of bio-oil (arrival and departure weights) or equivalent; Calibration records for scales | 7.4.1 (Bio-oil Geological Storage) |
| [math: m_{Tailgas}] | Mass flow rate of tail gas from biomass pyrolysis | Always | Eq. 8 (Bio-oil Geological Storage) | Measured or calculated | kg/hr |
|
|
|
|
| 7.4.3. |
| [math: C_{Tailgas,\ CO_{2}}] | Concentration of CO2 in tailgas | Always | Eq. 8 (Bio-oil Geological Storage) | Measured | wt% |
|
|
|
|
| 7.4.3. |
| [math: C_{Tailgas,\ CH_{4}}] | Concentration of CH4 in tailgas | Always | Eq. 8 (Bio-oil Geological Storage) | Measured | wt% |
|
|
|
|
| 7.4.3. |
| [math: t_{p}] | Biomass conversion batch operation time | Always | Eq. 8 (Bio-oil Geological Storage) | Measured | hr | Operator logs or automated plant data acquisition system / historian | Data historian time stamp or operator timing / stopwatch | Each batch | Review of batch duration and validation of batch production time | Operator logs or data from plant data historian | 7.4.3. |
| [math: m_{fuel,\ conversion}] | Mass of fuel used in biomass conversion | Always | Eq. 5 (Energy Use Accounting Module) | Measured | gal | Fuel usage records |
| Each batch | Appropriate calibration and maintenance of scales or meters | Operator logs, plant data systems, or plant records | 7.4.3. |
| [math: EF_{Fuel, Conversion}] | Fuel emission factor for biomass conversion | Always | Eq. 5 (Energy Use Accounting Module) | Estimated | CO2e/unit (tonnes) | Argonne National Laboratory GREET Model, California Air Resources Board modified GREET model (CA-GREET), Ecoinvent database, US Federal Life Cycle Inventory database or LCA Commons, or from similar databases used in common LCA practices or tools | N/A | Each batch | N/A | Choice and rationale for EF choice | 7.4.3. |
| [math: kwh_{Conversion}] | Electricity usage for biomass conversion | Always | Eq. 2 (Energy Use Accounting Module) | Measured | kwh | Electricity usage records |
| Each batch | Appropriate calibration and maintenance of meters | Operator logs, plant data systems, or plant records | Section 7.4.3. |
| [math: EF_{Elect, Conversion}] | Electricity emission factor | Always | Eq. 2 (Energy Use Accounting Module) | Estimated | CO2e/kwh (tonnes) | Argonne National Laboratory GREET Model, California Air Resources Board modified GREET model (CA-GREET), Ecoinvent database, US Federal Life Cycle Inventory database or LCA Commons, or from similar databases used in common LCA practices or tools | N/A | Each batch | N/A | Choice and rationale for EF choice | 7.4.3. |
| [math: F_{Conversion}] | Quantity of fuel used in transport of biomass to conversion site | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Measured or estimated | gal | Vehicle or fleet management records | Fuel flow meters, fleet management system data, vehicle on board diagnostics, or similar | All deliveries for a batch | Verify instrument calibrations as appropriate | Meter, management system, OBD or other data records or logs, shipping documents | 7.4.3. |
| [math: F_{Injection}] | Quantity of fuel used in transport of bio-oil to injection site | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Measured or estimated | gal | Vehicle or fleet management records | Fuel flow meters, fleet management system data, vehicle on board diagnostics, or similar | All deliveries for a batch | Verify instrument calibrations as appropriate | Meter, management system, OBD or other data records or logs, shipping documents | 7.4.3. |
| [math: EF_{Fuel, Transportation}] | Fuel emission factor for transportation | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Estimated | CO2e/unit (tonnes) | Argonne National Laboratory GREET Model, California Air Resources Board modified GREET model (CA-GREET), Ecoinvent database, US Federal Life Cycle Inventory database or LCA Commons, or from similar databases used in common LCA practices or tools | N/A | All trips for each batch | N/A | Choice and rationale for EF choice | 7.4.3. |
| [math: D_{Conversion}] | Biomass transportation distance traveled - feedstock supplier to conversion site | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Measured or estimated | mi or km |
| On-line mapping systems using origin and departure from shipping documents, odometer readings | All trips for each batch | Review and check of shipping records and origin/destination | Shipping records | Section 7.4.3. |
| [math: W_{Conversion}] | Mass of biomass transported from supplier to conversion site | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Measured | kg, tonne, lb |
| Calibrated weigh scale | All deliveries for a batch | Review weigh scale calibration certificate | Shipping records, weigh scale ticket | Section 7.4.3. |
| [math: D_{Injection}] | Bio-oil transportation distance traveled - conversion site to injection site | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Measured or estimated | mi or km |
| On-line mapping systems using origin and departure from shipping documents, odometer readings | All trips for each batch | Review and check of shipping records and origin/destination | Shipping records | Section 7.4.3. |
| [math: W_{Injection}] | Mass of bio-oil transported from conversion site to injection site | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Measured | kg, tonne, lb |
| Calibrated weigh scale | All deliveries for a batch | Review weigh scale calibration certificate | Shipping records, weigh scale ticket | Section 7.4.3. |
| [math: EF_{Transportation, j}] | The weight- and distance-based emission factor for transportation | Under certain conditions | Eq. 2 (Transportation Emissions Accounting Module) | Estimated | CO2e/unit (tonnes) | Argonne National Laboratory GREET Model, California Air Resources Board modified GREET model (CA-GREET), Ecoinvent database, US Federal Life Cycle Inventory database or LCA Commons, or from similar databases used in common LCA practices or tools | N/A | All trips for each batch | N/A | Choice and rationale for EF choice | 7.4.3. |
| [math: m_{fuel,\ Injection}] | Mass of fuel used in bio-oil injection | Always | Eq. 5 (Energy Use Accounting Module) | Measured | gal | Fuel usage records |
| Each batch | Appropriate calibration and maintenance of scales or meters | Operator logs, plant data systems, or plant records | Section 7.4.3. |
| [math: EF_{Fuel, Injection}] | Fuel emission factor for bio-oil injection | Always | Eq. 5 (Energy Use Accounting Module) | Estimated | CO2e/unit (tonnes) | Argonne National Laboratory GREET Model, California Air Resources Board modified GREET model (CA-GREET), Ecoinvent database, US Federal Life Cycle Inventory database or LCA Commons, or from similar databases used in common LCA practices or tools | N/A | Each batch | N/A | Choice and rationale for EF choice | 7.4.3. |
| [math: kwh_{Injection}] | Electricity usage for bio-oil injection | Always | Eq. 2 (Energy Use Accounting Module) | Measured | kwh | Electricity usage records |
| Each batch | Appropriate calibration and maintenance of meters | Operator logs, plant data systems, or plant records | Section 7.4.3. |
| [math: EF_{Elect, Injection}] | Electricity emission factor | Always | Eq. 2 (Energy Use Accounting Module) | Estimated | CO2e/kwh (tonnes) | Argonne National Laboratory GREET Model, California Air Resources Board modified GREET model (CA-GREET), Ecoinvent database, US Federal Life Cycle Inventory database or LCA Commons, or from similar databases used in common LCA practices or tools | N/A | Each batch | N/A | Choice and rationale for EF choice | 7.4.3. |
| Product Stage Emissions | Includes raw material sourcing, transport to facility and manufacturing | Always | Measured | tonnes | Independently verified LCAs for the material or product completed; an environmental product declaration (EPD) for a material or product completed and independently verified | Number/weight of each product or material used in the project facility and a corresponding EPD-based embodied carbon emission factor, OR emission factors from LCA life cycle databases, including USLCI database, Ecoinvent, ICE Database, and other published and peer-reviewed databases of embodied emissions factors and the number or weight (depending on emission factor units) of each product or material at the facility, OR overall total cost of equipment and facilities for the project and cost based embodied emission factors | Each site | ISO 14040 or similar guidelines; ISO 14025, ISO 21930, EN 15804 or equivalent standards including product EPDs as well as industry-wide EPDs | Operator logs, plant data systems, or plant records | 7.4.3. | |
| Construction Stage Emissions | Includes transport to site and installation at site | Always | Measured | tonnes | Independently verified LCAs for the material or product completed; or an environmental product declaration (EPD) for a material or product completed and independently verified | Number/weight of each product or material used in the project facility and a corresponding EPD-based embodied carbon emission factor, OR emission factors from LCA life cycle databases, including USLCI database, Ecoinvent, ICE Database, and other published and peer-reviewed databases of embodied emissions factors and the number or weight (depending on emission factor units) of each product or material at the facility, OR overall total cost of equipment and facilities for the project and cost based embodied emission factors | Each site | ISO 14040 or similar guidelines; ISO 14025, ISO 21930, EN 15804 or equivalent standards including product EPDs as well as industry-wide EPDs | Operator logs, plant data systems, or plant records | 7.4.3. | |
| End of Life Stage Emissions | Includes demolition of building, transport to end of life, waste processing and final disposal or scenarios for these life cycle stages | Always | Measured | tonnes | Independently verified LCAs for the material or product completed; an environmental product declaration (EPD) for a material or product completed and independently verified | Number/weight of each product or material used in the project facility and a corresponding EPD-based embodied carbon emission factor, OR emission factors from LCA life cycle databases, including USLCI database, Ecoinvent, ICE Database, and other published and peer-reviewed databases of embodied emissions factors and the number or weight (depending on emission factor units) of each product or material at the facility, OR overall total cost of equipment and facilities for the project and cost based embodied emission factors | Each site | ISO 14040 or similar guidelines; ISO 14025, ISO 21930, EN 15804 or equivalent standards including product EPDs as well as industry-wide EPDs | Operator logs, plant data systems, or plant records | 7.4.3. | |
| Storage and Monitoring Emissions | The total quantity of GHG emissions associated with storage monitoring operations allocated to a removal | Always | Measured | tonnes | Electricity and fuel usage records; independently verified LCAs for the material or product completed; an environmental product declaration (EPD) for a material or product completed and independently verified | Electricity meters OR utility bills OR equipment time of use and power rating; fuel meters fuel container weight fuel purchases or utility bills equipment hours of operation (handling equipment only) | Each site | Appropriate calibration and maintenance of scales or meters | Operator logs, plant data systems, or plant records | 7.4.3. |
ASTM D5291-21 Standard Test Methods for Instrumental Determination of Carbon, Hydrogen, and Nitrogen in Petroleum Products and Lubricants. (2021, November). https://www.astm.org/standards/d5291
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Carbon Direct & EcoEngineers. (2022). Bio-oil Sequestration Prototype Protocol for Measurement, Reporting, & Verification. https://d13en5kcqwfledinsights.cloudfrontcarbon-direct.netcom/fileshubfs/Bio-oil-proto-protocol.pdf
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Sustainable sourcing may be demonstrated via certification or demonstrated compliance with programs such as the Forest Stewardship Council (https://fsc.org/en), High Conservation Value Network (https://www.hcvnetwork.org/), Sustainable Biomass Program (https://sbp-cert.org/), Roundtable for Sustainable Biomass (https://rsb.org/the-rsb-standard/about-the-rsb-standard/), European Union Renewable Energy Directive (RED II), Sustainable Forestry Initiative, or other similar biomass sustainability protocols, standards, and compliance methods. ↩
Note that other well classes may be utilized, such as Class II wells, if site specific UIC well permits identify bio-oil as an acceptable injectant. However, Class II wells may not be utilized if the wells are also used for enhanced hydrocarbon recovery (EHR or EHR+) activities. ↩
For Class V wells, the well must be permitted and not ‘authorized by rule’, and must consider the specific emplacement and durable storage of bio-oil in the geologic reservoir. As of writing, the utilization of Class V wells should be limited to wells operating under the Other / Experimental category of Class V wells or other appropriate well type as approved by the UIC permitting authority. ↩
https://www.nrel.gov/docs/fy22osti/80967.pdf↩↩2
https://www.nist.gov/pml/owm/publications/nist-handbooks/handbook-44-current-edition↩
Flow meters must be calibrated to national traceable standards by an ISO 17025 accredited metrology laboratory. Flow meters may include critical nozzle flow meters (i.e. ISO 9300:2022 compliant meters), coriolis mass flow meters, and other applicable meters for mixed gas flows, as long as properly calibrated and maintained. ↩