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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.

Mustang Station Power Plant

Natural GasFEED· University of Texas at Austin· 2022-01-07Project page ↗Cost report ↗
CO₂ captured
853,644t/yr
Capture efficiency
90.0%
Utilization
52.0%
Parasitic load
46MW
CO₂ concentration
3.8%vol%
Facility scope
EngineeringAECOM
Point source approachPost-Combustion Capture
CO₂ concentration3.8% vol%
Flue gas pressure14 psia
Compressor nameplate
Compression stages3
Compression inlet75 psia
Compression discharge2,015 psia
Description
The University of Texas at Austin, with AECOM Technical Services and Trimeric Corporation, is conducting a FEED study for the Piperazine Advanced Stripper (PZAS) CO₂ capture process at Golden Spread Electric Cooperative’s Mustang Station in Denver City, Texas. Designed for two GE gas turbines with HRSGs and a steam turbine totaling 464 MWe, the PZAS process uses 30 wt% piperazine for higher efficiency, solvent stability, smaller absorber size, and cost savings compared to conventional amine systems. The project will deliver a 30–60% complete design package and a capital cost estimate with ±15% accuracy.

Linde / Port Arthur Facility

Hydrogenpre-FEED· Linde· 2023-12-04Project page ↗Cost report ↗
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.

Cleveland Cliffs / Burns Harbor

Iron and Steelpre-FEED· Dastur International· 2023-03-01Project page ↗Cost report ↗
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.