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Carbon Capture Costs: FEED & pre-FEED Cost Reports

Carbon capture costs from pre-FEED and FEED studies across power, cement, steel, natural gas, hydrogen and other industrial sectors. Browse capital (capex) and operating (opex) cost estimates from publicly available engineering reports, drill down into cost buckets and line items, and compare up to three projects side-by-side.

3 of 3 selectedClear selection46 reports
Comparing 3 reports — tab selection applies to every column.

CRC / Elk Hills Power Plant

Natural GasFEED· Electric Power Research Institute (EPRI)· 2020-09-01Project page ↗Cost report ↗
CO₂ captured
1,460,000t/yr
Capture efficiency
90.0%
Utilization
95.0%
Parasitic load
35MW
CO₂ concentration
4.3%mol%
Facility scope
EngineeringFluor
Point source approachPost-Combustion Capture
CO₂ concentration4.3% mol%
Flue gas pressure15 psia
Compressor nameplate
Compression stages7
Compression inlet
Compression discharge2,315 psia
Description
Electric Power Research Institute (EPRI), with Fluor Corporation and California Resources Corporation (CRC), conducted a FEED study to assess the feasibility of retrofitting Fluor’s solvent for post-combustion CO₂ capture at the 550 MW Elk Hills NGCC power plant. The system aims to capture approximately 4,000 tonnes of CO₂ per day (75% of total emissions, or 90% of an 83% slipstream), with the captured CO₂ intended for enhanced oil recovery. Deliverables include the full engineering design package—such as process flow diagrams, equipment datasheets, and capital cost estimates—optimized for site-specific performance, operations, and construction practices.

Finnish Market Pulp Mill / Capture of CO2 in the Lime Kiln only

Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
197,008t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
2.8MW
CO₂ concentration
27.6%mol%
Facility scope
Engineering
Point source approachPost-Combustion Capture
CO₂ concentration27.6% mol%
Flue gas pressure
Compressor nameplate
Compression stages4
Compression inlet
Compression discharge1,595 psia
Description
Analysis sets the design and cost-estimating basis for evaluating pulp and board mills with and without CCS. Two base cases are considered: a market pulp mill and an integrated pulp and board mill. Six CCS cases are evaluated, capturing CO₂ from the recovery boiler, multi-fuel boiler, lime kiln, or their combinations. The mills are assumed to be energy independent, with black liquor and bark burned to produce steam and electricity, and excess electricity exported to the grid. The CO₂ capture system uses post-combustion MEA technology with a 90% capture rate, and if on-site electricity is insufficient, an auxiliary boiler firing forest residues will supply the additional energy. Capture of CO2 in the Lime Kiln only

Gerald Gentleman Station

CoalFEED· ION Clean Energy· 2023-03-01Project page ↗Cost report ↗
CO₂ captured
4,316,020t/yr
Capture efficiency
89.8%
Utilization
85.0%
Parasitic load
MW
CO₂ concentration
Facility scope
EngineeringSargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration
Flue gas pressure
Compressor nameplate
Compression stages6
Compression inlet
Compression discharge2,115 psia
Description
ION Clean Energy, with Nebraska Public Power District, is conducting a FEED study to retrofit a CO₂ capture system on Unit 2 of the 700 MWe Gerald Gentleman Station in Nebraska. Using ION’s low-aqueous ICE-21 solvent, proven in prior DOE-funded projects to reduce energy use, solvent degradation, and emissions, the design will feature two parallel 350 MWe capture units. The project aims to decarbonize most of Unit 2 while maintaining maximum operational flexibility for the plant.