Tools
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.
Comparing 3 reports — tab selection applies to every column.
Southern Company / Plant Daniel
CO₂ captured
1,769,520t/yr
Capture efficiency
90.0%
Utilization
—
Parasitic load
79MW
CO₂ concentration
—
Facility scope
EngineeringLinde Engineering (ISBL), Southern Company Services (OSBL)
Point source approachPost-Combustion Capture
CO₂ concentration—
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Southern Company Services, with Linde Gas North America, is conducting a FEED study for a commercial-scale CO₂ capture system using Linde-BASF’s advanced aqueous amine technology at an NGCC plant of at least 375 MWe. The project will evaluate Alabama Power’s Plant Barry and Mississippi Power’s Plant Daniel to select the optimal host site, define project requirements, optimize process design, and deliver engineering packages along with a cost and schedule estimate within 15% accuracy. The study will build on prior feasibility work and site-specific testing.
Linde Hydrogen Plant
CO₂ captured
1,360,000t/yr
Capture efficiency
95.0%
Utilization
—
Parasitic load
—MW
CO₂ concentration
18.3%mol%
Facility scope
EngineeringLinde Engineering
Point source approachPost-Combustion Capture
CO₂ concentration18.3% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Linde Inc., with Linde Engineering Americas and BASF, is conducting an initial engineering design for a 3,500 tonnes/day CO₂ capture plant using Linde-BASF’s advanced aqueous amine technology at a Linde-owned steam methane reforming facility. The project will define integration options, establish project requirements, optimize process design, and develop engineering, cost, and schedule packages. BASF will provide the technology design, LEA will deliver detailed engineering and constructability assessments, and Linde will lead techno-economic, environmental, and safety analyses in coordination with the SMR plant operators.
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.