How to Calculate Direct Air Capture Regeneration Energy
Regeneration energy demand determines whether a direct air capture (DAC) facility can achieve its promised cost and carbon intensity. Thermal requirements dominate the operating budget for solid sorbent systems, while auxiliary electricity for blowers, vacuum pumps, and compression adds a non-trivial share. Investors, heat suppliers, and offtakers increasingly request transparent calculations that reconcile process data with design guarantees.
This guide codifies a rigorous methodology for estimating regeneration energy. We define the variables, map the equations, and provide a workflow you can adapt from pilot scale to commercial deployments. The approach complements sorbent productivity benchmarking covered in the sorbent productivity walkthrough and integrates smoothly with the market-based Scope 2 emissions guide to ensure carbon disclosures reflect actual utility consumption.
Definition and system boundaries
Regeneration energy is the thermal and electrical energy required to release captured CO₂ from sorbent beds and prepare the gas for compression or storage. The boundary typically includes the desorption heaters, vacuum systems, sorbent handling, and post-release conditioning (for example, moisture knock-out). For solid sorbent DAC, thermal energy is often supplied as steam, hot oil, or resistive heating. Auxiliary loads comprise fans moving ambient air through contactors, vacuum pumps that lower pressure during desorption, and compressors that deliver CO₂ to pipeline pressure.
Fix the boundary before calculating. Decide whether to include parasitic loads such as cooling water pumps, CO₂ polishing, or site utilities. Align the boundary with financial models and sustainability accounting so the regeneration figure reconciles with project economics and emissions factors.
Variables, symbols, and units
Document the following inputs and outputs with SI units:
- mCO₂ – Net CO₂ captured per day (t/day). Use custody-transfer measurements after accounting for vent losses.
- eth – Specific regeneration thermal energy (GJ/t). Derived from process design, pilot tests, or heat balance simulations.
- frec – Heat recovery fraction (%). Portion of the regeneration heat recovered via recuperation, heat pumps, or integration with other processes.
- eaux – Auxiliary electricity per tonne (kWh/t). Includes blowers, vacuum pumps, conveyors, and compression as defined by the system boundary.
- Eth,gross – Gross thermal energy demand (MWh/day). Equals mCO₂ × eth ÷ 3.6.
- Eth,net – Net thermal energy after recovery (MWh/day).
- Eaux – Auxiliary electric energy (MWh/day).
- Etot – Total regeneration energy (MWh/day).
- etot – Net specific regeneration energy (MWh/t).
Express heat recovery as a decimal (for example, 0.20 for 20%) when applying it inside formulas. If your recovery system has multiple stages, calculate a weighted average or handle each stage separately before aggregating results.
Deriving the regeneration energy equations
Start with the gross thermal load, which scales the specific energy by the capture rate and converts gigajoules to megawatt-hours:
Eth,gross = (mCO₂ × eth) ÷ 3.6
Eth,net = Eth,gross × (1 − frec)
Eaux = (mCO₂ × eaux) ÷ 1,000
Etot = Eth,net + Eaux
etot = Etot ÷ mCO₂
The 3.6 divisor converts gigajoules to megawatt-hours (1 MWh = 3.6 GJ). Auxiliary electricity uses 1,000 to convert kilowatt-hours to megawatt-hours. When eaux covers compression to sequestration pressure, validate the conversion against compressor polytropic efficiency curves.
You can extend the model by splitting auxiliary loads into categories—air moving, vacuum, compression—and assigning unique improvement roadmaps. Integrate waste heat utilisation scenarios or thermal storage from the pumped thermal storage efficiency guide when pairing DAC with grid services.
Step-by-step calculation workflow
1. Fix the capture rate and timeframe
Use the net captured mass over a consistent period—daily is typical for utility planning. Adjust for commissioning ramp, downtime, or sorbent change-outs so the rate reflects sustainable operation.
2. Source specific regeneration energy
Pull eth from heat and mass balance simulations or vendor performance guarantees. If only cycle energy (per batch) is available, convert to per tonne by dividing by the mass of CO₂ released each cycle.
3. Quantify heat recovery
Evaluate recuperators, mechanical vapour recompression, or thermal storage that recycles heat between stages. Base frec on measured exchanger effectiveness or design-stage pinch analysis. Keep a conservative default until the recovery system proves its performance.
4. Catalogue auxiliary electricity
Sum the electrical loads for blowers, pumps, vacuum systems, conveyors, and compressors. Convert peak power to energy by multiplying by operating hours. Distinguish between baseload and duty-cycled loads so you can prioritise efficiency retrofits.
5. Execute the calculation and document assumptions
Input the values into the formulas or use the embedded calculator. Record data sources, measurement timestamps, and any adjustments (for example, derating fans for altitude). Store everything in a shared repository for audit and financing due diligence.
Validation and scenario analysis
Cross-check Etot against actual utility bills or historian exports. If measured energy deviates by more than ±5%, reconcile instrumentation accuracy, unmetered loads, or unplanned downtime. Compare etot to peer benchmarks from technology roadmaps or public demonstrations to ensure your figures align with industry expectations.
Run scenarios by flexing frec (for example, 0%, 20%, 40%) and evaluating the impact on heat supply agreements. Evaluate the sensitivity of CO₂ removal cost by pairing Etot with fuel or electricity price forecasts. These insights feed into financing decisions and into carbon intensity calculations used in the LLM inference carbon intensity methodology when cross-sector comparisons are required.
Limits and interpretation guidance
The calculation assumes steady-state operation and average values for heat recovery and auxiliary loads. Transient effects—startup surges, sorbent degradation, ambient weather swings—may shift energy demand temporarily. Incorporate safety margins when sizing heat sources or procuring renewable electricity contracts.
Remember that heat quality matters. Delivering the required megawatt-hours at insufficient temperature will fail to regenerate sorbent effectively. Document minimum temperature requirements alongside the energy balance to prevent mismatched supply agreements.
Embed: Direct air capture regeneration energy calculator
Enter capture rate, specific regeneration energy, heat recovery, and auxiliary electricity to obtain daily thermal load, auxiliary demand, total energy, and per-tonne intensity in one step.