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.
Milton R. Young Power Plant
CO₂ captured
4,297,145t/yr
Capture efficiency
90.0%
Utilization
85.0%
Parasitic load
83.3MW
CO₂ concentration
8.6%vol%
Facility scope
EngineeringFluor
Point source approachPost-Combustion Capture
CO₂ concentration8.6% vol%
Flue gas pressure—
Compressor nameplate44.4 MW
Compression stages—
Compression inlet—
Compression discharge1,690 psia
Description
Milton R. Young Station Unit 2 is conducting a FEED study to add a post-combustion CO₂ capture system using Fluor’s Econamine FG Plus™ technology to its lignite-fueled power plant in North Dakota. The design targets 3.6 million tonnes of CO₂ captured annually—twice the scale of the largest existing facility—while integrating advanced heat recovery, aerosol and solvent degradation controls, and cold-climate optimization to achieve the lowest levelized cost of capture at world scale. The study will deliver detailed design, cost, and performance data for financing, permitting, and final project scheduling.
Technology Centre Mongstad
CO₂ captured
5,658,960t/yr
Capture efficiency
70.0%
Utilization
85.0%
Parasitic load
182MW
CO₂ concentration
12.5%mol%
Facility scope
EngineeringTrimeric
Point source approachPost-Combustion Capture
CO₂ concentration12.5% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages6
Compression inlet6 psia
Compression discharge2,219 psia
Description
Membrane Technology and Research Inc., with Technology Centre Mongstad, Dresser-Rand, Trimeric Corporation, and WorleyParsons/Advisian, is scaling up its advanced Polaris™ membranes for post-combustion CO₂ capture and testing them at engineering scale at TCM in Norway. The Polaris membranes, about 20 times more permeable than prior commercial versions, use a patented selective recycle design to boost CO₂ concentration in flue gas and lower capture costs. The project will design, build, and operate a modular membrane system for a six-month field test, including performance verification, steady-state operation, techno-economic updates, and integration studies with advanced compression technology.
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.