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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.

3 of 3 selectedClear selection46 reports
Comparing 3 reports — tab selection applies to every column.

Devon Energy / Jackfish-1 Oil Sands

Natural GasFEED· Devon Energy· 2011-11-01Project page ↗Cost report ↗
CO₂ captured
365,000t/yr
Capture efficiency
90.0%
Utilization
85.0%
Parasitic load
MW
CO₂ concentration
8.6%mol%
Facility scope
EngineeringHTC Puretech
Point source approachPost-Combustion Capture
CO₂ concentration8.6% mol%
Flue gas pressure15 psia
Compressor nameplate
Compression stages
Compression inlet
Compression discharge
Description
A Front End Engineering and Design (FEED) study was undertaken to design an advanced CO2 Capture Unit (CCU) to produce 1000 tonnes per day of CO2 from the exhaust of three Once-Through Steam Generators (OTSG’s) at Devon Energy’s Jackfish 1 thermal in-situ operations and estimate the capital expenditure for the facilities within +/-15% accuracy. The process utilizes HTC Purenergy Carbon Capture Technology to capture CO2 from the OTSG exhaust gas using an aqueous chemical solvent in an absorber tower, after which the CO2-loaded solvent is passed to a stripper tower where the CO2 is released and the solvent regenerated. The study excludes downstream CO2 compression, dehydration, transportation and storage.

Finnish Market Pulp Mill / Capture of CO2 in the Kraft Recovery Boiler only

Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
1,478,700t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
23.5MW
CO₂ concentration
14.7%mol%
Facility scope
Engineering
Point source approachPost-Combustion Capture
CO₂ concentration14.7% 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 the Kraft Recovery Boiler only

Phillips 66 / Rodeo Refinery

Hydrogenpre-FEED· Phillips 66 Company· 2023-08-09Project page ↗Cost report ↗
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.