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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.

CEMEX / Balcones Cement Plant

Cementpre-FEED· Sargent and Lundy· 2026-01-01Cost report ↗
CO₂ captured
2,400,000t/yr
Capture efficiency
95.0%
Utilization
74.0%
Parasitic load
MW
CO₂ concentration
12.8%mol%
Facility scope
EngineeringSargent and Lundy
Point source approachPost-Combustion Capture
CO₂ concentration12.8% mol%
Flue gas pressure14 psia
Compressor nameplate46 MW
Compression stages5
Compression inlet
Compression discharge2,215 psia
Description
The CEMEX Balcones Carbon Capture project is a DOE-supported Front-End Engineering Design (FEED) study evaluating commercial-scale deployment of RTI International’s non-aqueous solvent (NAS) technology at the Balcones cement plant in New Braunfels, Texas. The study assessed capture of approximately 2.4 million tonnes of CO₂ per year at roughly 95% capture efficiency from cement kiln flue gas and an associated natural gas–fired boiler, developing an AACE Class 3 cost estimate and detailed engineering design to support future investment decisions. Led by RTI International with KBR as EPC engineering contractor and SLB Capturi as owner’s engineer and technology licensor, the project evaluated integration challenges such as limited cooling water availability, resulting in a hybrid air- and water-cooling configuration. The FEED estimated total project capital costs of about $849 million and annual operating costs of approximately $109 million, providing a techno-economic basis for large-scale cement decarbonization and future project execution planning.

Red Trail Energy Richardton Ethanol

Ethanol· Trimeric· 2019-11-20Project page ↗Cost report ↗
CO₂ captured
214,255t/yr
Capture efficiency
Utilization
95.9%
Parasitic load
MW
CO₂ concentration
99.9%mol%
Facility scope
EngineeringTrimeric
Point source approachEthanol
CO₂ concentration99.9% mol%
Flue gas pressure
Compressor nameplate3.8 MW
Compression stages28
Compression inlet
Compression discharge365 psia
Description
The Red Trail Energy (RTE) ethanol facility in Richardton, North Dakota, is implementing a CO₂ capture and liquefaction system designed by Trimeric. The system captures CO₂ from fermentation, compresses it to ~350 psig, dehydrates and liquefies it using an ammonia refrigeration loop, and purifies it via distillation to remove oxygen and other gases. The liquid CO₂ can be stored for sale or geologic sequestration. The facility is designed to process 587 tonnes/day (scalable to 675 tonnes/day), with nearly complete CO₂ recovery.

Southern Company / Plant Barry

Natural GasFEED· GE Gas Power· 2024-08-06Project page ↗Cost report ↗
CO₂ captured
1,632,000t/yr
Capture efficiency
95.0%
Utilization
85.0%
Parasitic load
18.4MW
CO₂ concentration
6.7%mol%
Facility scope
EngineeringLinde Engineering (process engineering and equipment cost), Kiewit (plant layout, constructability, installation)
Point source approachPost-Combustion Capture
CO₂ concentration6.7% mol%
Flue gas pressure14 psia
Compressor nameplate20.8 MW
Compression stages
Compression inlet
Compression discharge2,215 psia
Description
General Electric Gas Power, with Linde, Kiewit, and Southern Company Services, is conducting a FEED study for a “Generation 2” amine-based post-combustion CO₂ capture system at an existing NGCC power plant. Targeting at least 95% capture efficiency, the design will emphasize optimized integration, lower CCS costs, and flexible operation to complement renewable energy. The 18-month project will progress from multiple conceptual designs to a single configuration, culminating in a detailed design, technical viability assessment, techno-economic and life cycle analyses, and a business case evaluation.