CostingEnergy mass balanceEquipment sizingCarbon capture
Modular amine post-combustion CO2 capture unit
Amine capture on industrial flue gas (boiler, cement, incinerator): regeneration heat, electricity, amine make-up, scaled CAPEX and cost of CO2 captured in EUR/t, on the Danish Energy Agency 401.a datasheet, sized in t/d like the CO2 liquefaction calculator.
- CurrencyEUR 2025
- Battery limitfully financed
- 77 documented assumptions
- Updated27 Oct 2026
Mass and energy balance
What the asset draws and delivers for the case and load you choose.
Reference case
Share of the year at nameplate capture. Default 90 % is the GCCSI 2025 cost basis. It follows the operation of the emitter.
Flows
- In: Electricity (capture and compression)—
- In: LP steam to the reboiler—
Asset
Modular amine post-combustion CO2 capture unit
- Out: Captured CO2—
Annual quantities at the current usage. Outline: full capacity, 8,760 h. Fill: 90.0 % capacity factor. Band width: share of energy in; non-energy flows are not to scale.
Nameplate CO2 captured per day. Default 768 t/d is the DEA 401.a anchor (32 t/h). The CAPEX follows a 0.6 scale law sourced on built plants of 240 to 4,800 t/d (10-200 t/h, DEA): below 240 t/d, where MHI CO2MPACT (up to 200 t/d) and the smallest CycloneCC trains (from 75 t/d) sit, the law is extrapolated and the result is flagged.
- Capture capacity per hour
- — t/h
- Reboiler heat duty at full load
- — MW
- Electric load at full load
- — MW
- CycloneCC trains of 855 t/d
- — trains
CAPEX
Specific cost at this size, what backs it, and how it behaves with scale.
Specific CAPEX at this size
—
Reference size 768 t/d
DEA CCTS p.15, GCCSI 2025 p.27
Model value: the DEA case scaled to the capacity. Customized: your own all-in specific CAPEX (a vendor quote for a modular unit), used as is at every size and no longer sourced.
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- Ex-factory
- Installed
- Fully financed· this figure
Included
- Equipment and installation
- Indirect and owner's costs
- Contingency
Not included
- Nothing
Added at project level
- Nothing: project mode uses the figure as is
Project figures
Values passed to project mode when this asset is added to a project.
Modular amine post-combustion CO2 capture unitConcept sketch, not to scale · drag to rotate
- Electricity (capture and compression) in
- —
- LP steam to the reboiler in
- —
- Captured CO2 outMain product
- —
- CAPEX to the battery limit
- —
- Fixed O&M
- —
- Variable O&M, excluding feedstocks
- —
- Asset lifetime
- 25 years
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Cost of CO2 captured
A standalone indicator for a quick read. Project mode recomputes it for the whole system.
—
- Capture cost - capital—
- Capture cost - fixed O&M—
- Capture cost - variable O&M—
- Capture cost - reboiler steam—
- Capture cost - electricity—
Linked to the balance above
Share of the year at nameplate capture. Default 90 % is the GCCSI 2025 cost basis. It follows the operation of the emitter.
Included: compression and dehydration to 150 bar for pipeline transport (100 kWh/t, DEA Table 4). Not included: CO2 leaves the stripper near atmospheric pressure, for example to the liquefaction calculator; 0.2 MEUR per t/h is taken off the CAPEX (low end of DEA's 0.2-0.5).
CO2 in the flue gas, %vol. 15 % is the DEA biomass/waste CHP reference; cement kilns run about 20 %, gas turbines 3-4 %. Below 6 % the reboiler heat rises by 15 % (DEA: 10-15 %); above it DEA sees only a marginal effect.
Share of the CO2 in the treated flue gas that is captured. DEA 2025: 90 %. It sets the CO2 left in the flue gas and the flue gas treated; DEA gives no energy or cost law for other rates, so those stay at the 90 % values.
Price of the gas burnt to raise LP steam. Default 60.5 EUR/MWh is the Eurostat EU non-household average for S2 2025. Set 0 if the reboiler runs on waste heat that is genuinely free.
Default 183.7 EUR/MWh is the Eurostat EU non-household average for S2 2025.
Real rate, as a fraction (0.095 = 9.5 %). Costs are in constant EUR. With the DEA 25-year life, 9.5 % gives a CRF of 10.6 %, the value GCCSI 2025 uses for its captured costs.
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Benchmarks
This model's figures against published references and reference cases.
Regeneration heat, GJ/t
2.1 IEAGHG 2018-TR03 p.45
2.5 DEA CCTS Table 6
2.8 IEAGHG 2018-TR03 p.45
3.5 DEA CCTS Table 6
4.1 IEAGHG 2018-TR03 p.45
Capture-unit electricity, kWh/t
20 DEA CCTS Table 6
40 DEA CCTS Table 6
Compression electricity, kWh/t
90 DEA CCTS Table 4
120 DEA CCTS Table 4
Capital recovery factor (%), %
10.6 GCCSI 2025 p.38
Reference cases at this size and usage
Log in to compare the reference cases.
All results
Every model output at the current settings, grouped, with the sensitivity charts.
53 outputs · 4 groups · 19 also shown above, dimmed
Cost of CO2 captured
10- Cost of CO2 captured with free waste heat
- ComputingEUR/t
- Energy share of the capture cost
- Computing%
- LP steam cost
- ComputingEUR/GJ
- Total annual cost
- ComputingEUR/year
Capital and O&M
17- Total CAPEX
- ComputingMEUR
- Reference specific CAPEX at 768 t/d
- ComputingEUR/(t/d)
- Specific CAPEX at this size (DEA unit)
- ComputingMEUR/(t/h)
- Specific CAPEX with exponent 0.8
- ComputingEUR/(t/d)
- Compression CAPEX - low
- ComputingMEUR
- Compression CAPEX - high
- ComputingMEUR
- Capital recovery factor
- Computing1/year
- CRF gap to GCCSI 2025
- Computing%
- Annualised CAPEX
- ComputingEUR/year
- Variable O&M per t
- ComputingEUR/t
- Steam cost per year
- ComputingEUR/year
- Electricity cost per year
- ComputingEUR/year
Energy
15- Regeneration heat before low-CO2 penalty
- ComputingGJ/t
- Low-CO2 heat penalty
- Computing%
- Dilute flue gas
- Computingbool
- Specific electricity
- ComputingkWh/t
- Compression electricity - GCCSI cross-check
- ComputingkWh/t
- Total energy use per t
- ComputingGJ/t
- Reboiler heat per year
- ComputingGJ/year
- Reboiler heat per year (MWh)
- ComputingMWh/year
- Electricity per year
- ComputingMWh/year
Mass balance and sizing
11- Equivalent full-load hours
- Computingh/year
- CO2 captured per year
- Computingt/year
- CO2 in the treated flue gas
- Computingt/year
- CO2 left in the flue gas
- Computingt/year
- Flue gas treated per t captured
- Computingt/t
- Flue gas treated per year
- Computingt/year
- Amine make-up
- Computingkg/t
- Amine make-up per year
- Computingt/year
- Outside the sourced size range
- Computingbool
Sensitivities
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Sources
77 documented assumptions · 6 sources
- ens.dkDanish Energy Agency & Energinet, Technology Data CCTS, datasheet 401.a 'Post comb - small CHP' (2025 est.)investment, O&M, heat, electricity, amine, lifetime
- ens.dkDanish Energy Agency, Technology Data for Carbon Capture, Transport and Storagescale exponent (p.15), compression (Table 4), Table 6, typical capacities (p.37)
- globalccsinstitute.comGlobal CCS Institute, Advancements in CCS Technologies and Costs (2025)CRF 10.6 %, 90 % capacity factor, scale exponent 0.6-0.8, compressor power
- publications.ieaghg.orgIEAGHG 2018-TR03, Cost of CO2 Capture in the Industrial SectorMEA and advanced amine regeneration energy
- ec.europa.euEurostat, natural gas and electricity price statistics, EU non-household S2 2025
- energy.govUS DOE AMO, Steam Tip Sheet #15natural gas boiler combustion efficiency 85.7 %
About
Calculator context
About
Calculator context
A screening model of a post-combustion amine capture unit on industrial flue gas (biomass or waste boiler, cement kiln, incinerator), built for a feasibility study that has to stand in front of a lender. Every number comes from one dated public catalogue, the Danish Energy Agency and Energinet datasheet 401.a 'Post comb - small CHP' (2025 estimate), whose three columns (estimate, lower, upper) are the three reference cases: specific investment 5.9 / 3.54 / 8.26 MEUR per t CO2/h at 32 t/h, reboiler steam 0.833 / 0.66 / 1.0 MWh/t, capture electricity 30 / 25 / 35 kWh/t, variable O&M 2.5 / 1.5 / 3.5 EUR/t with the amine make-up inside, fixed O&M 3 % of CAPEX, 25-year life. The DEA scope includes liquefaction; this calculator stops at 150 bar compression (100 kWh/t, DEA Table 4) and removes the 0.2 MEUR per t/h DEA gives for that difference (note J). Liquefaction is the separate calculator, chained on the same t/d.
The size is the CO2 captured per day. The CAPEX follows a 0.6 scale law (DEA: 0.6-0.7; GCCSI 2025: 0.6-0.8) from the 768 t/d anchor. DEA reports built plants of 10-200 t/h, so the law is sourced from 240 t/d upward; between 1 and 240 t/d, where MHI CO2MPACT and the smallest CycloneCC trains sit, it is extrapolated, the 'Outside the sourced size range' flag is raised and the charts stop at 240 t/d. A vendor quote goes in as a Customized CAPEX. The reboiler duty rises by 15 % below 6 %vol CO2 in the flue gas (DEA: 10-15 % at 3-4 %), and is otherwise flat with CO2 content, as DEA states.
At the DEA central case and 768 t/d, 90 % capacity factor, compression on, EU non-household gas (60.5 EUR/MWh, Eurostat S2 2025) and electricity (183.7 EUR/MWh), the cost of CO2 captured is 183.5 EUR/t: 76.6 capital, 21.7 fixed O&M, 2.5 variable O&M, 58.8 steam (3.0 GJ/t at 19.6 EUR/GJ from an 85.7 % gas boiler) and 23.9 electricity (130 kWh/t). The CAPEX is 182.4 MEUR. The annuity uses a 9.5 % real rate over 25 years, a CRF of 10.60 %, the 10.6 % GCCSI 2025 uses. With free waste heat the cost falls to 124.7 EUR/t. At the DEA upper column, 240 t/d and a 3 %vol flue gas it is 334.5 EUR/t.
Read it with its limits: a cost per tonne captured, not avoided (the CO2 of the steam and power is not deducted); constant prices; the capture rate changes the CO2 left in the flue gas and the gas treated, not the energy or CAPEX per tonne, since DEA gives no law for other rates; the blower power is not re-scaled with the flue gas volume. The CAPEX is the DEA all-in figure and is exported as fully financed, so project mode adds no further cost layer.
Model
127 variables — inputs, calculations and outputs, with their dependencies.
Model
127 variables — inputs, calculations and outputs, with their dependencies.
| Variable | Value | Unit | Depends on |
|---|---|---|---|
| 768 | t/d | — | |
| 90 | % | — | |
| 1 | — | — | |
| 0 | — | — | |
| 237500 | EUR/(t/d) | — | |
| 1 | — | — | |
| 15 | % | — | |
| 90 | % | — | |
| 60.5 | EUR/MWh | — | |
| 183.7 | EUR/MWh | — | |
| 0.095 | ratio | — |
| Variable | Formula | Unit | Depends on |
|---|---|---|---|
if((<=)+(<=)+(>)+(!=)*(!=)*(!=)+(<)+(>)+(>=)*(<=)+(<=)+(>)+(<=)+(>)+(<)+(>)+(<)+(<)+(<)+(>=)>,,) | bool | ||
if(==,,if(==,,))--(-)* | MEUR/(t/h) | ||
if(>=,,) | — | ||
if(>=,,) | EUR/(t/d) |
| Variable | Formula | Unit | Depends on |
|---|---|---|---|
/ | t/h | ||
** | h/year | ||
* | t/year | ||
/max(*,) | t/year | ||
- | t/year | ||
*(/max(,))*(/max(,)) | t/t | ||
* | t/year | ||
if(<,,) | bool | ||
* | % | ||
if(==,,if(==,,))* | GJ/t | ||
*(+*) | GJ/t | ||
if(==,,if(==,,)) | kWh/t | ||
*if(==,,if(==,,)) | kWh/t | ||
+ | kWh/t | ||
+* | GJ/t | ||
* | GJ/year | ||
/ | MWh/year | ||
** | MWh/year | ||
*/ | MW | ||
** | MW | ||
* | GJ/year | ||
if(==,,if(==,,)) | kg/t | ||
** | t/year | ||
*/ | EUR/(t/d) | ||
clamp(*(/)^(-),,) | EUR/(t/d) | ||
*/ | MEUR/(t/h) | ||
*(/)^(-) | EUR/(t/d) | ||
* | EUR | ||
/ | MEUR | ||
** | MEUR | ||
** | MEUR | ||
if(<,/,(*(+)^)/max((+)^-,)) | 1/year | ||
* | % | ||
- | % | ||
* | EUR/year | ||
** | EUR/year | ||
if(==,,if(==,,)) | EUR/t | ||
* | EUR/year | ||
/max(*,)/ | EUR/GJ | ||
* | EUR/year | ||
* | EUR/year | ||
/max(,) | EUR/t | ||
/max(,) | EUR/t | ||
/max(,) | EUR/t | ||
/max(,) | EUR/t | ||
/max(,) | EUR/t | ||
++++ | EUR/t | ||
++++ | EUR/year | ||
(+)/max(,)* | % | ||
- | EUR/t | ||
if((<)+(>*)>,,) | bool | ||
ceil(/) | trains | ||
*/ | kWh/t |
Assumptions
77 assumptions used in the calculations
Assumptions
77 assumptions used in the calculations
Protects divisions against a zero denominator; small enough to leave every result unchanged.
Market range Not applicable (numerical or unit constant).
0.000001Numerical constantLiteral zero for guards and flags, so no number is written inline.
Market range Not applicable (numerical or unit constant).
0Numerical constantLiteral one for flags, the CRF and multipliers.
Market range Not applicable (numerical or unit constant).
1Numerical constantConverts a percent input (0-100) to a fraction.
Market range Not applicable (numerical or unit constant).
0.01Numerical constantConverts a fraction to percent.
Market range Not applicable (numerical or unit constant).
100%Numerical constantConverts t/d to t/h (and M EUR per t/h to EUR per t/d).
Market range Not applicable (numerical or unit constant).
24h/dNumerical constantHours in a non-leap year; base of the load hours.
Market range Not applicable (numerical or unit constant).
8760h/yearNumerical constantDays in a non-leap year.
Market range Not applicable (numerical or unit constant).
365d/yearNumerical constant1 MWh = 3.6 GJ (DEA prints heat in MWh/t, this calculator shows GJ/t).
Market range Not applicable (numerical or unit constant).
3.6GJ/MWhNumerical constant1 kWh = 0.0036 GJ.
Market range Not applicable (numerical or unit constant).
0.0036GJ/kWhNumerical constant1 kWh = 0.001 MWh.
Market range Not applicable (numerical or unit constant).
0.001MWh/kWhNumerical constant1 kg = 0.001 t.
Market range Not applicable (numerical or unit constant).
0.001t/kgNumerical constant1 million EUR.
Market range Not applicable (numerical or unit constant).
1000000EUR/MEURNumerical constantInteger id of the reference case 'DEA 401.a 2025 central estimate' in the technology_case select; no string in the DSL.
Market range Not applicable (selector).
1Selector idInteger id of the reference case 'DEA 401.a 2025 lower column' in the technology_case select; no string in the DSL.
Market range Not applicable (selector).
2Selector idInteger id of the reference case 'DEA 401.a 2025 upper column' in the technology_case select; no string in the DSL.
Market range Not applicable (selector).
3Selector idSize of the DEA cost anchor. The sourced specific investment is per (t CO2/h) at this size.
Market range Single anchor size in the datasheet.
32t/hDEA Technology Data CCTS, datasheet 401.aReference size of the CAPEX scale law, in the size unit of the slider (t/d). Also the default size.
Market range Single anchor size in the datasheet.
768t/dDEA datasheet 401.a, converted to t/dCAPEX = C_ref x (size / 768 t/d)^0.6, so the specific CAPEX per t/d scales with exponent 0.6 - 1 = -0.4. 0.6 is the low end of both sources: it gives the strongest economy of scale, hence the highest specific cost for small modules. DEA states the law for the whole plant; it does not give a separate exponent for compact or modular units.
Market range0.6DEA CCTS p.15, GCCSI 2025 p.27Upper end of the GCCSI exponent band. Used only in the 'specific CAPEX at exponent 0.8' check output, to show how much the small-module cost depends on the exponent.
Market range0.8GCCSI 2025 p.27Lower edge of the size range DEA reports for built plants. Below it the 0.6 scale law is extrapolated: no public source found covers the CAPEX of amine modules below 10 t/h.
Market range10t/hDEA CCTS p.37Upper edge of the DEA size range (4,800 t/d), above the slider maximum.
Market range200t/hDEA CCTS p.37Below 240 t/d the out-of-sourced-domain flag is raised and the CAPEX is an extrapolation of the 0.6 law.
Market range 10 t/h = 240 t/d.
240t/dDEA CCTS p.37, converted to t/dLower clamp of the scaled specific CAPEX. Far below any value the law reaches on the 1-1,000 t/d slider (the lowest is about 118,000 EUR/(t/d), at 1,000 t/d in the DEA lower case without compression), so it never binds inside the slider range; it only stops a non-physical value outside it.
Market range Not applicable (guard).
1000EUR/(t/d)Numerical guardUpper clamp of the scaled specific CAPEX. Above the highest value the law reaches on the slider (about 4.8 million EUR/(t/d) at 1 t/d in the DEA upper case), so it never binds inside the slider range.
Market range Not applicable (guard).
100000000EUR/(t/d)Numerical guardCentral DEA specific investment. Scope includes liquefaction, which this calculator does not (liquefaction is the separate chainable calculator), so note J's 0.2 is removed.
Market range Lower 3.54, upper 8.26 MEUR/(t/h) (same sheet).
5.9MEUR/(t/h)DEA datasheet 401.aSpecific investment of the 'DEA lower' reference case, before removing liquefaction.
Market range3.54MEUR/(t/h)DEA datasheet 401.aSpecific investment of the 'DEA upper' reference case, before removing liquefaction.
Market range8.26MEUR/(t/h)DEA datasheet 401.aRemoved from every DEA case: the scope of this calculator stops at 150 bar compression (or at the stripper outlet if compression is off). 5.9 - 0.2 = 5.7 MEUR/(t/h) capture + compression.
Market range Single value in note J.
0.2MEUR/(t/h)DEA datasheet 401.a note JRemoved when compression is switched off. The low end of the DEA range is taken so as not to over-deduct: the DEA plant cost already integrates compression with the capture unit and its share is not split in the datasheet.
Market range0.2MEUR/(t/h)DEA CCTS Table 4Upper end of the compression CAPEX range, shown in the compression CAPEX range output.
Market range0.5MEUR/(t/h)DEA CCTS Table 4Fixed O&M per year = 3 % of the CAPEX, in every reference case.
Market range Single value (DEA).
3%DEA CCTS p.49Variable O&M of the central case. It contains the amine make-up (about 2 EUR/t) and small consumables (0.5 EUR/t, DEA p.49); amine is therefore not counted again.
Market range2.5EUR/tDEA datasheet 401.aVariable O&M of the 'DEA lower' case.
Market range1.5EUR/tDEA datasheet 401.aVariable O&M of the 'DEA upper' case.
Market range3.5EUR/tDEA datasheet 401.aPart of the central variable O&M that is amine make-up. Documents why amine is not costed a second time; not added to the cost.
Market range Not split for the lower/upper columns.
2EUR/tDEA CCTS p.49Solvent make-up for degradation and losses, central case. Information only (its cost sits in variable O&M).
Market range0.3kg/tDEA datasheet 401.aSolvent make-up of the 'DEA lower' case.
Market range0.15kg/tDEA datasheet 401.aSolvent make-up of the 'DEA upper' case (MEA-like degradation).
Market range1.5kg/tDEA datasheet 401.aReboiler LP steam per t of CO2 captured, central case (0.833 x 3.6 = 3.0 GJ/t), for a flue gas with 15 %vol CO2.
Market range0.833MWh/tDEA datasheet 401.aReboiler heat of the 'DEA lower' case (2.38 GJ/t).
Market range0.66MWh/tDEA datasheet 401.aReboiler heat of the 'DEA upper' case (3.6 GJ/t).
Market range1MWh/tDEA datasheet 401.aBelow 6 %vol CO2 in the flue gas the low-CO2 penalty applies. DEA documents a step between two regimes, not a continuous law, so the model uses a step at the low end of the 6-8 % band.
Market range6%DEA CCTS p.32Low end of the DEA low-CO2 penalty; shown in the penalty range, not used in the cost.
Market range10%DEA CCTS p.32Penalty applied to the reboiler heat when the flue gas is below 6 %vol CO2. The high end is used so that a dilute stream is not under-costed in front of a lender.
Market range15%DEA CCTS p.32Benchmark: low end of the DEA technology-chapter range for the reboiler duty.
Market range2.5GJ/tDEA CCTS Table 6Benchmark: high end of the DEA technology-chapter range.
Market range3.5GJ/tDEA CCTS Table 6Benchmark: low end of the MEA reboiler duty in an independent source.
Market range2.8GJ/tIEAGHG 2018-TR03 p.45Benchmark: high end of the MEA reboiler duty (older MEA plants).
Market range4.1GJ/tIEAGHG 2018-TR03 p.45Benchmark: best advanced-amine reboiler duty reported by IEAGHG.
Market range 2.1 GJ/t (advanced amine).
2.1GJ/tIEAGHG 2018-TR03 p.45Capture-unit electricity of the central case, without compression.
Market range30kWh/tDEA datasheet 401.aCapture-unit electricity of the 'DEA lower' case.
Market range25kWh/tDEA datasheet 401.aCapture-unit electricity of the 'DEA upper' case.
Market range35kWh/tDEA datasheet 401.aBenchmark: low end of the DEA technology-chapter range for capture electricity.
Market range20kWh/tDEA CCTS Table 6Benchmark: high end of the DEA technology-chapter range for capture electricity.
Market range40kWh/tDEA CCTS Table 6Compression and dehydration to 150 bar, central case; added when compression is on.
Market range100kWh/tDEA CCTS Table 4Compression electricity of the 'DEA lower' case.
Market range90kWh/tDEA CCTS Table 4Compression electricity of the 'DEA upper' case.
Market range120kWh/tDEA CCTS Table 4Independent cross-check of the DEA compression figure. Converted by this calculator (not printed by GCCSI): 3,784 kW x 24 h / 1,000 t = 90.8 kWh/t, at the low end of the DEA 90-120.
Market range Single design point.
3784kWGCCSI 2025 Table 4Capacity at which GCCSI gives the compressor power; used only to convert it to kWh/t.
Market range Single design point.
1000t/dGCCSI 2025 Table 4Capture rate at which DEA gives its flue gas mass per t captured; reference of the flue gas scaling. The capture-rate slider defaults to it.
Market range 90 % (DEA 2025); 85-95 % on the slider.
90%DEA datasheet 401.aFlue gas CO2 concentration of the DEA reference; reference of the flue gas scaling and the slider default.
Market range15%DEA datasheet 401.aFlue gas treated per t captured at the DEA reference. Scaled by 15 / CO2 %vol and 90 / capture rate: at a constant mean molar mass of the flue gas, the mass of gas per t of CO2 is inversely proportional to the CO2 volume fraction. Information only; the blower electricity is not re-scaled (DEA gives no split).
Market range Single value at 15 %vol.
5.1t/tDEA datasheet 401.aDefault of the capacity factor slider (also used to read the GCCSI cost basis).
Market range90%GCCSI 2025 p.38Physical service life of the capture plant; annuity period of the CRF and lifetime exported to project mode.
Market range 25 years (DEA).
25yearsDEA datasheet 401.aBenchmark of the CRF. GCCSI does not state the rate and the period in the quoted text; this calculator computes its own CRF from the discount rate and the DEA 25-year life, and shows the gap to 10.6 %.
Market range Single value (GCCSI).
10.6%GCCSI 2025 p.38Default real discount rate 9.5 %: over the DEA 25 years it gives a CRF of 10.60 %, the GCCSI value. This is a calibration of one free parameter on one published factor, declared as such. All costs are in constant EUR with no escalation, so the rate is read as real.
Market range 0-12 % on the slider.
—Calibrated on GCCSI 2025Default of the gas price slider (60.5 EUR/MWh).
Market range EU non-household average; national prices vary widely.
0.0605EUR/kWhEurostatDefault of the electricity price slider (183.7 EUR/MWh).
Market range EU non-household average; large consumers often pay less.
0.1837EUR/kWhEurostatConverts the gas price to a steam cost: EUR/GJ steam = gas price / 0.857 / 3.6. At 60.5 EUR/MWh gas the steam costs 19.6 EUR/GJ. Set the gas price to 0 for genuinely free waste heat.
Market range Single benchmark value.
85.7%DOE Steam Tip Sheet #15Catalog product: largest CO2MPACT size, inside the extrapolated range (below 240 t/d).
Market range200t/dMHI 2024Catalog product: smallest CycloneCC train, inside the extrapolated range.
Market range75t/dCarbon CleanLargest CycloneCC train; used to count how many trains of that size the capacity needs.
Market range855t/dCarbon CleanCost of CO2 captured = (CAPEX x CRF + fixed O&M) / t captured per year + variable O&M + reboiler heat x steam cost + electricity x price. It is a captured cost, not an avoided cost: the CO2 emitted to make the steam and electricity is not deducted.
Market range Not applicable (method).
—DEA 401.a, GCCSI 2025Scope: capture unit with flue gas pre-treatment, utilities, cooling water and optional compression and dehydration to 150 bar. Liquefaction (about 0.16 MWh/t), transport and storage are outside; flue gas desulphurisation upstream is assumed done by the host.
Market range Not applicable (scope).
—DEA 401.aBetween 1 and 240 t/d the 0.6 law is extrapolated below the smallest DEA plant size, where the catalog products sit (MHI CO2MPACT up to 200 t/d, CycloneCC from 75 t/d). The flag 'Outside the sourced size range' is raised and the charts are drawn on 240-1,000 t/d only. Packaged modular units may cost less than this extrapolation suggests; a vendor quote belongs in the Customized CAPEX.
Market range Not applicable (limit).
—DEA CCTS p.37The reboiler duty only responds to the flue gas CO2 through the documented low-CO2 step (below 6 %vol). The capture rate changes the CO2 in the flue gas and the flue gas mass, not the energy or the CAPEX per t captured: DEA gives no law for capture rates other than 90 %.
Market range Not applicable (limit).
—DEA CCTS p.32