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.
Holcim / Portland Cement Plant
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).
Finnish Market Pulp Mill / Capture of CO2 in the Multi-fuel Boiler only
Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
270,658t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
4.4MW
CO₂ concentration
16.8%mol%
Facility scope
Engineering—
Point source approachPost-Combustion Capture
CO₂ concentration16.8% mol%
Flue gas pressure—
Compressor nameplate—
Compression stages4
Compression inlet—
Compression discharge1,595 psia
Description
Analysis sets the design and cost-estimating basis for evaluating pulp and board mills with and without CCS. Two base cases are considered: a market pulp mill and an integrated pulp and board mill. Six CCS cases are evaluated, capturing CO₂ from the recovery boiler, multi-fuel boiler, lime kiln, or their combinations. The mills are assumed to be energy independent, with black liquor and bark burned to produce steam and electricity, and excess electricity exported to the grid. The CO₂ capture system uses post-combustion MEA technology with a 90% capture rate, and if on-site electricity is insufficient, an auxiliary boiler firing forest residues will supply the additional energy. Capture of CO2 in the Multi-fuel Boiler only
Red Trail Energy Richardton Ethanol
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.