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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.

Holcim / Portland Cement Plant

Cementpre-FEED· Electricore· 2023-01-31Project page ↗Cost report ↗
CO₂ captured
1,733,750t/yr
Capture efficiency
90.0%
Utilization
Parasitic load
76MW
CO₂ concentration
10.1%vol%
Facility scope
EngineeringKiewit
Point source approachPost-Combustion Capture
CO₂ concentration10.1% vol%
Flue gas pressure
Compressor nameplate
Compression stages7
Compression inlet
Compression discharge2,230 psia
Description
Electricore Inc., with Svante Inc. and Kiewit Engineering Group Inc., is conducting a pre-FEED study for a 1 million tonnes/year VeloxoTherm™ carbon capture system at LafargeHolcim’s cement plant in Florence, Colorado. The system will capture CO₂ from both kiln flue gas (14% concentration) and a natural gas-fired steam generator (8.5% concentration), with storage options including saline formations, depleted oil reservoirs, and the Sheep Mountain CO₂ reservoir. The study will also evaluate expansion to 2 million tonnes/year and target DOE’s $30/tonne capture cost goal, progressing from design selection (FEL-1) to pre-FEED engineering (FEL-2).

Southern Company / Plant Barry

Compression and Dehydration· Trimeric· 2020-02-01Project page ↗Cost report ↗
CO₂ captured
4,200,000t/yr
Capture efficiency
Utilization
95.0%
Parasitic load
MW
CO₂ concentration
99.0%vol%
Facility scope
EngineeringTrimeric
Point source approachCompression and Dehydration
CO₂ concentration99.0% vol%
Flue gas pressure
Compressor nameplate43.3 MW
Compression stages8
Compression inlet30 psia
Compression discharge1,515 psia
Description
This report summarizes Trimeric’s Phase II work under the SSEB ECO2S project in Kemper County, Mississippi, focused on Task 7 – Infrastructure Development. Trimeric evaluated CO₂ compression and dehydration costs, compared pumping versus compression for dense phase CO₂, and developed pipeline transport cost estimates. Using experience from past projects, screening-level designs and cost estimates were prepared for a nominal 1 MTPY case and scaled to site-specific conditions. Results showed that increasing discharge pressure modestly raises costs, with pumping offering slight savings and operational flexibility but added complexity. Pipeline costs were estimated using NPC benchmarks, while compression and dehydration costs were scaled for Plant Daniel, Plant Miller, and Kemper. Overall, capital costs were roughly three times equipment costs, with electricity for compression as the dominant operating expense. The costs are associated with 8-stage compression to 1,500 psig

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.