Carbon Capture, Utilisation
& Storage (CCUS)
TTS v1.0 - Annex C
CCUS captures fossil-origin CO₂ directly from industrial point sources - cement kilns, steel blast furnaces, hydrogen reformers, and fossil power plants - before it reaches the atmosphere, then permanently stores it geologically or incorporates it into long-lived materials. As an avoided-emissions pathway rather than an atmospheric removal pathway, CCUS issues Reduction credits and plays a central decarbonisation role for hard-to-abate industrial sectors that have few lower-carbon production alternatives.
Submit CCUS Project View TTS v1.0 Annex C →How this pathway works
Carbon Capture, Utilisation and Storage captures CO₂ directly at the point of industrial emission - before dilution into the wider atmosphere - using post-combustion, pre-combustion, or oxy-fuel capture chemistry matched to the facility's process design. Cement kilns face a particular challenge unique among industrial emitters: roughly half of cement process CO₂ comes from the calcination of limestone itself, a chemical reaction with no fossil-fuel-switching alternative, making capture the primary decarbonisation lever for the sector.
Under the Teravent Technology-Based Carbon Standard (TTS v1.0) Annex C, CCUS projects earn Teravent Technology Credits of the Reduction type (TTC-D) for verified net tonnes of industrial CO₂ captured and either permanently stored (via the Annex G geological storage protocol) or incorporated into long-lived materials, net of full lifecycle project emissions. Because the CO₂ source is fossil or process-origin rather than atmospheric or biogenic, CCUS credits represent avoided emissions rather than atmospheric removal - an important distinction credit buyers should understand when selecting a claim type.
Five methodology variants are approved under Annex C, spanning the three principal capture chemistries (post-combustion, pre-combustion, oxy-fuel) plus a cement-specific process emissions methodology and a materials-utilisation route. Each specifies its own capture energy penalty, storage or utilisation route, and sector-specific baseline.
TTS v1.0 - Annex C
This pathway is governed exclusively by the Teravent Technology-Based Carbon Standard (TTS v1.0). No external registry, standard, or methodology is referenced or incorporated. All requirements - additionality, quantification, durability, safeguards, and credit issuance - are defined within TTS v1.0, Annex C, and - where geological storage is selected - the shared storage requirements of Annex G.
Five approved methodology variants
TTS v1.0 Annex C approves five discrete methodology types for the CCUS pathway, spanning capture chemistry and end-of-capture destination. A facility may combine capture methodology with either storage route (geological, per Annex G) or a materials utilisation route (CCU-M05), but must declare the selected destination at registration since it determines durability class and buffer requirements.
Post-combustion capture retrofits an amine scrubbing unit (or equivalent solvent-based system) to an existing facility's flue gas stack, capturing CO₂ after combustion is complete without modifying the core combustion process. This is the most widely deployable CCUS methodology, applicable across fossil power generation, cement kilns, steel blast furnaces, and refineries, and is the default retrofit route for existing industrial assets.
- Continuous CO₂ capture rate at scrubber outlet via calibrated metering, ±2% accuracy
- Solvent regeneration steam/heat consumption logged for lifecycle energy penalty deduction
- Facility fuel input and baseline (uncontrolled) emissions factor documented per sector-specific protocol
- Amine solvent degradation and make-up rate, with any solvent emissions to atmosphere assessed under DNSH air quality provisions
- Selected storage or utilisation route monitoring per Annex G or CCU-M05 respectively
Pre-combustion capture applies to facilities that convert a fossil fuel into syngas (a hydrogen and CO mixture) before combustion or synthesis - steam methane reforming for hydrogen production, or integrated gasification combined cycle (IGCC) power generation. The water-gas shift reaction converts CO to CO₂, which is then separated using pressure-swing adsorption or physical solvent scrubbing at higher partial pressure than post-combustion flue gas, typically achieving lower capture energy penalty per tonne.
- Continuous CO₂ capture rate at syngas separation outlet, ±2% accuracy
- Feedstock (natural gas, coal) input rate and carbon content per batch
- Co-product output (hydrogen, ammonia, power) tracked for lifecycle emissions allocation
- Water-gas shift conversion efficiency and unconverted CO slip to atmosphere
- Selected storage or utilisation route monitoring per Annex G or CCU-M05 respectively
Oxy-fuel combustion replaces ambient air with a near-pure oxygen stream (produced via air separation unit) for fuel combustion, eliminating atmospheric nitrogen dilution and producing a flue gas that is predominantly CO₂ and water vapour. After water condensation, the resulting stream requires only compression and drying rather than chemical solvent-based separation, at the cost of the substantial electricity required to produce the oxygen stream.
- Continuous CO₂ capture rate at post-condensation outlet via calibrated metering, ±2% accuracy
- Air separation unit electricity consumption logged for lifecycle energy penalty deduction
- Oxygen purity and combustion efficiency at the boiler or kiln
- Technology Readiness Level documentation updated at each verification for TRL-based additionality screening
- Selected storage or utilisation route monitoring per Annex G or CCU-M05 respectively
Cement production emits CO₂ from two distinct sources: fuel combustion in the kiln, and the chemical calcination of limestone (CaCO₃ → CaO + CO₂) - a reaction with no fuel-switching alternative, typically responsible for roughly 50–60% of a cement plant's total process emissions. This methodology applies capture technology (often post-combustion or oxy-fuel, per CCU-M01/M03) specifically calibrated to address both the combustion and process emissions streams together, since cement kiln exhaust combines both sources in a single flue gas stream requiring separate baseline treatment.
- Continuous CO₂ capture rate apportioned between calcination process emissions and fuel combustion emissions
- Clinker production volume and raw meal composition per batch, for process emissions factor calculation
- Alternative fuel (waste-derived fuel) co-firing rate, since this changes the combustion-source emissions baseline
- Where captured CO₂ is used in concrete curing, overlap check against Annex J to prevent double-registration
- Selected storage or utilisation route monitoring per Annex G or CCU-M05/Annex J respectively
Rather than geological injection, this methodology covers captured CO₂ that is chemically incorporated into a durable end product - polymers, mineral aggregates, or other long-lived carbon-embedding materials - where the CO₂ is bound within the material's molecular or crystalline structure for the duration of the product's service life. This methodology governs the utilisation-side accounting only; where the resulting material is itself a registered Teravent pathway (e.g. CO₂ Concrete Curing under Annex J, or Synthetic Carbon Materials under Annex I), the utilisation must be registered under that pathway instead to avoid double registration.
- CO₂ mass incorporated per unit of finished product, verified by material composition analysis
- Independent engineering service-life assessment for the specific product and application
- Product distribution and end-use tracking to prevent double counting of embodied-carbon claims by downstream purchasers
- End-of-life disposition monitoring - landfill, incineration, or recycling - since this affects long-term carbon retention
- Confirmation the same mineralised or incorporated tonnes are not separately registered under Annex I or Annex J
Which emission sources must be counted
TTS v1.0 Module 3 requires a full lifecycle GHG emissions inventory within the project boundary, deducted from gross captured CO₂ to arrive at the Net TTC figure. Sector-specific process emissions factors (particularly for cement) must be used rather than generic industry averages.
Measurement, reporting
& verification
Teravent's Science Advisory Board assesses each pathway against four MRV dimensions. CCUS benefits from decades of industrial gas metering experience, giving very high capture quantification confidence, though sector-specific baseline determination - particularly for cement process emissions - introduces some additionality complexity.
CO₂ capture is quantified via continuous flow metering at ±2% accuracy at the capture system outlet, with source apportionment required where a facility has both process and combustion emissions streams (notably cement, CCU-M04). Sector-specific baseline emissions factors - clinker-specific for cement, per-tonne-of-steel for blast furnaces, per-unit-output for power - must be applied rather than generic defaults, and updated as facility efficiency or fuel mix changes. Where CO₂ is routed to geological storage, monitoring follows the Annex G protocol; where routed to materials utilisation (CCU-M05), an independent engineering service-life assessment substitutes for subsurface monitoring.
Demonstrating additionality
TTS v1.0 Module 2 requires all projects to pass a three-test additionality framework. For CCUS, the regulatory surplus test carries particular weight and complexity, given an increasing number of jurisdictions now mandate or incentivise carbon capture for new industrial construction in hard-to-abate sectors.
Leakage types & deductions
TTS v1.0 Module 3 defines three leakage types applicable across all engineered pathways. CCUS is primarily subject to energy-source leakage and production-shifting leakage, the latter reflecting the risk that a facility subject to capture costs may lose market share to uncontrolled competitors.
Buffer pool & reversal risk
CCUS durability depends entirely on the selected storage or utilisation route. Geologically stored CO₂ (via Annex G) carries Class III permanence; materials-incorporated CO₂ (CCU-M05) carries Class II permanence, reflecting the shorter and more variable service life of manufactured products relative to geological formations.
| Methodology / Route | Durability Class | Buffer Pool Rate | Primary Reversal Risks |
|---|---|---|---|
| CCU-M01–M04 + Geologic Storage | Class III | 2–15% | Storage complex reversal per Annex G SIRR assessment |
| CCU-M05 Materials Utilisation | Class II | 7–25% | Product end-of-life disposal releasing embedded CO₂; shorter/uncertain service life |
| CCU-M04 + Concrete Curing (Annex J) | Class III | 2–8% | Confirmed carbonate mineral formation in cured concrete; low reversal risk once cured |
Key registration criteria
Projects must meet all of the following minimum requirements to qualify for registration under TTS Annex C. Additional methodology-specific requirements are detailed in the Annex C methodology tables for each CCU-M code.
Sustainable Development
Goal alignment
All Teravent registered CCUS projects must complete an SDG impact assessment at registration and at each verification period. Three SDGs are systematically tracked for this pathway, reflecting its role in industrial decarbonisation and the associated workforce transition. Projects may apply for co-benefit quality labels where independently verified indicators are met.
Deployment scope: Global - wherever cement, steel, hydrogen, and fossil power facilities operate, with the greatest decarbonisation urgency in regions with concentrated heavy industry and limited access to cleaner production alternatives.
Ready to register your
CCUS project?
Submit a Project Concept Note under TTS v1.0 Annex C to begin your registration. Select the CCU-M code matching your capture chemistry, choose a storage or utilisation route, install continuous CO₂ metering, and appoint an accredited VVB to validate your PDD.