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.
CEMEX / Balcones Cement Plant
CO₂ captured
744,235t/yr
Capture efficiency
75.0%
Utilization
90.0%
Parasitic load
36MW
CO₂ concentration
14.9%vol%
Facility scope
EngineeringSargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration14.9% vol%
Flue gas pressure14 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge2,213 psia
Description
Membrane Technology & Research Inc., with Sargent & Lundy and CEMEX, is designing a full-scale Polaris membrane CO₂ capture system for the CEMEX Balcones cement plant in New Braunfels, Texas, targeting about 1 million tonnes of CO₂ capture annually. The study will develop the design basis, process design, cost estimates, permitting and safety reviews, constructability assessment, and a techno-economic analysis. Sargent & Lundy will lead the design work, while CEMEX will provide site-specific data for integration.
Finnish Integrated Pulp and Board Mill / Capture of CO2 in both Kraft Boiler & Lime Kiln
Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
1,675,922t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
26.9MW
CO₂ concentration
15.5%mol%
Facility scope
Engineering—
Point source approachPost-Combustion Capture
CO₂ concentration15.5% 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 Boiler & Lime Kiln
Phillips 66 / Rodeo Refinery
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.