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.
Cleveland Cliffs / Burns Harbor
CO₂ captured
2,800,000t/yr
Capture efficiency
95.0%
Utilization
—
Parasitic load
79MW
CO₂ concentration
21.9%vol%
Facility scope
EngineeringDastur International
Point source approachPost-Combustion Capture
CO₂ concentration21.9% vol%
Flue gas pressure17 psia
Compressor nameplate—
Compression stages6
Compression inlet—
Compression discharge2,215 psia
Description
Dastur International Inc., with Cleveland-Cliffs Inc., is designing a carbon capture system for the 5 mtpa integrated steel plant in Burns Harbor, Indiana, to capture 50–70% of CO₂ emissions from blast furnace gas. The system will combine a gas flow distribution network, a specialized conditioning process, and ION Clean Energy’s solvent-based capture technology with 90–98% efficiency, with water-gas shift reactors enabling higher capture rates. Dastur will lead overall plant integration and engineering, while ION designs the capture island and Dastur Energy optimizes design and energy performance.
Gerald Gentleman Station
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.
Linde / Port Arthur Facility
CO₂ captured
1,435,000t/yr
Capture efficiency
92.0%
Utilization
90.0%
Parasitic load
—MW
CO₂ concentration
16.2%mol%
Facility scope
EngineeringKiewit (EPC costs for Svante’s equipment, steam generators, and OSBL construction), Linde (EPC costs for CO₂ purification/compression and EP costs for OSBL utilities)
Point source approachPost-Combustion Capture
CO₂ concentration16.2% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Linde Inc., with Linde Engineering Americas, Linde Engineering Dresden, and Svante Inc., is completing an initial engineering design for a commercial-scale CO₂ capture plant at its steam methane reforming hydrogen facility in Port Arthur, Texas. Using Svante’s VeloxoTherm™ solid adsorbent technology, the system will capture about 1 million tonnes of CO₂ annually at ≥90% efficiency while producing 99.97% pure “blue” hydrogen. The design will include ISBL units for flue gas conditioning and CO₂ purification, OSBL components, and a techno-economic analysis of capture costs and hydrogen production economics.