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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.

Gerald Gentleman Station

CoalFEED· ION Clean Energy· 2023-03-01Project page ↗Cost report ↗
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.

Phillips 66 / Rodeo Refinery

Hydrogenpre-FEED· Phillips 66 Company· 2023-08-09Project page ↗Cost report ↗
CO₂ captured
190,000t/yr
Capture efficiency
95.0%
Utilization
94.5%
Parasitic load
MW
CO₂ concentration
18.0%vol%
Facility scope
EngineeringWorley
Point source approachPre-Combustion Capture
CO₂ concentration18.0% vol%
Flue gas pressure20 psia
Compressor nameplate
Compression stages5
Compression inlet25 psia
Compression discharge2,250 psia
Description
Phillips 66, with Worley Group Inc., is developing the initial design for a commercial-scale CCS system at the Rodeo Refinery hydrogen plant, targeting over 90% capture efficiency and storage of about 190,000 tonnes of CO₂ annually. The project will evaluate three capture configurations—flue gas plus PSA tail gas, syngas plus flue gas, and flue gas only—selecting the most cost-effective option through a techno-economic analysis. The chosen design will be advanced to a level suitable for the next engineering phase, concluding with a final TEA for the selected CCS configuration.