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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.

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Comparing 3 reports — tab selection applies to every column.

CLECO / Brame Energy Center Madison 3 Unit

CoalFEED· Cleco Power· 2025-03-25
CO₂ captured
4,280,000t/yr
Capture efficiency
95.0%
Utilization
80.0%
Parasitic load
MW
CO₂ concentration
14.1%vol%
Facility scope
EngineeringSargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration14.1% vol%
Flue gas pressure15 psia
Compressor nameplate
Compression stages
Compression inlet
Compression discharge2,015 psia
Description
Cleco Power (Cleco) performed a three-phase front-end engineering and design (FEED) study evaluating installation of a carbon dioxide (CO2) Capture System at Madison Unit 3 (MU3), Project Diamond Vault (DV) The work was performed under a Department of Energy (DOE) grant DE-FE0032165. The FEED study included three phases: (1) a feasibility phase which sought to define the scope of the project, (2) a pre-FEED phase which sought to develop a detailed cost estimate, and (3) a final FEED phase which sought to develop the project to be ready to move into execution. The FEED study was completed by Cleco, Mitsubishi Heavy Industries America (MHIA), and Sargent & Lundy, LLC (S&L) with oversight provided by the Louisiana Economic Development (LED). The feasibility phase was completed in February 2023, which was followed by the pre-FEED phase which concluded in January 2024. The project subsequently entered the final FEED phase, during this phase Cleco made the decision to stop work on the FEED study due to market conditions which resulted in a project that was not economically viable at the time.

Finnish Market Pulp Mill / Capture of CO2 in the Multi-fuel Boiler only

Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
270,658t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
4.4MW
CO₂ concentration
16.8%mol%
Facility scope
Engineering
Point source approachPost-Combustion Capture
CO₂ concentration16.8% 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 Multi-fuel Boiler only

Finnish Market Pulp Mill / Capture of CO2 in both Kraft & Multi-boilers

Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
1,749,600t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
28.5MW
CO₂ concentration
15.0%mol%
Facility scope
Engineering
Point source approachPost-Combustion Capture
CO₂ concentration15.0% 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 both Kraft & Multi-boilers