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 Integrated Pulp and Board Mill / Capture of CO2 in Kraft, Multi-fuel Boilers & Lime Kiln
Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
1,946,575t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
31.4MW
CO₂ concentration
15.7%mol%
Facility scope
Engineering—
Point source approachPost-Combustion Capture
CO₂ concentration15.7% 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 Kraft, Multi-fuel Boilers & Lime Kiln
Linde / Port Arthur Facility
CO₂ captured
1,435,000t/yr
Capture efficiency
92.0%
Utilization
90.0%
Parasitic load
—MW
CO₂ concentration
16.2%mol%
Facility scope
EngineeringKiewit (EPC costs for Svante’s equipment, steam generators, and OSBL construction), Linde (EPC costs for CO₂ purification/compression and EP costs for OSBL utilities)
Point source approachPost-Combustion Capture
CO₂ concentration16.2% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Linde Inc., with Linde Engineering Americas, Linde Engineering Dresden, and Svante Inc., is completing an initial engineering design for a commercial-scale CO₂ capture plant at its steam methane reforming hydrogen facility in Port Arthur, Texas. Using Svante’s VeloxoTherm™ solid adsorbent technology, the system will capture about 1 million tonnes of CO₂ annually at ≥90% efficiency while producing 99.97% pure “blue” hydrogen. The design will include ISBL units for flue gas conditioning and CO₂ purification, OSBL components, and a techno-economic analysis of capture costs and hydrogen production economics.
Holcim / Ste. Genevieve Cement Plant
CO₂ captured
3,056,339t/yr
Capture efficiency
95.0%
Utilization
85.0%
Parasitic load
60MW
CO₂ concentration
20.3%mol%
Facility scope
EngineeringKiewit
Point source approachPost-Combustion Capture
CO₂ concentration20.3% mol%
Flue gas pressure16 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge2,215 psia
Description
The University of Illinois at Urbana-Champaign is leading a FEED study for a commercial-scale CO₂ capture system at Holcim’s Ste. Genevieve cement plant in Missouri, targeting 95% capture efficiency. Using Air Liquide’s Cryocap™ technology, which combines PSA pre-concentration with cryogenic purification, the system will produce high-purity CO₂ for storage near the Prairie State Generating Company in Illinois. UIUC will manage the project and perform economic and impact analyses, while Air Liquide, Kiewit, Visage Energy, and Holcim will contribute to design, safety, environmental, and site integration efforts.