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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.
Comparing 3 reports — tab selection applies to every column.
Technology Centre Mongstad
CO₂ captured
5,658,960t/yr
Capture efficiency
70.0%
Utilization
85.0%
Parasitic load
182MW
CO₂ concentration
12.5%mol%
Facility scope
EngineeringTrimeric
Point source approachPost-Combustion Capture
CO₂ concentration12.5% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages6
Compression inlet6 psia
Compression discharge2,219 psia
Description
Membrane Technology and Research Inc., with Technology Centre Mongstad, Dresser-Rand, Trimeric Corporation, and WorleyParsons/Advisian, is scaling up its advanced Polaris™ membranes for post-combustion CO₂ capture and testing them at engineering scale at TCM in Norway. The Polaris membranes, about 20 times more permeable than prior commercial versions, use a patented selective recycle design to boost CO₂ concentration in flue gas and lower capture costs. The project will design, build, and operate a modular membrane system for a six-month field test, including performance verification, steady-state operation, techno-economic updates, and integration studies with advanced compression technology.
Devon Energy / Jackfish-1 Oil Sands
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.
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.