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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.
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.
Nutrien Redwater Nitrogen Operations
CO₂ captured
1,778,645t/yr
Capture efficiency
99.0%
Utilization
—
Parasitic load
—MW
CO₂ concentration
7.0%mol%
Facility scope
EngineeringHatch
Point source approachPost-Combustion Capture
CO₂ concentration7.0% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge2,614 psia
Description
Studied the replacement of the SMR units with auto-thermal reforming (ATR) technology. ATRs produce a high concentration CO₂ stream, instead of low concentration combustion flue gases, that is more efficient to capture for sequestration. H₂ production from the unit may also be oversized to provide H₂ as a fuel source for the ATR if target overall CO₂ recovery of the facility is not achieved with the replacement of the SMR alone. The facility capacity is based on the total H₂ production requirements of the existing Plant 01 and Plant 09 ammonia synthesis units. 3 | P a g e Public – Approved for external distribution The scope for the study involves the SMR unit replacement with an integrated ATR and downstream syngas purification including CO₂ capture. The project scope also includes an Air Separation Unit (ASU) to supply oxygen to the ATR unit.
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.