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.
Finnish Market Pulp Mill / Capture of CO2 in the Lime Kiln only
Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
197,008t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
2.8MW
CO₂ concentration
27.6%mol%
Facility scope
Engineering—
Point source approachPost-Combustion Capture
CO₂ concentration27.6% 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 Lime Kiln only
Finnish Integrated Pulp and Board Mill / Capture of CO2 in both Kraft & Multi-boilers
Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
1,749,600t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
28.5MW
CO₂ concentration
15.0%mol%
Facility scope
Engineering—
Point source approachPost-Combustion Capture
CO₂ concentration15.0% 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 both Kraft & Multi-boilers
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).