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
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.
Calpine / Deer Park Energy Center
CO₂ captured
500,000t/yr
Capture efficiency
95.0%
Utilization
85.0%
Parasitic load
30.4MW
CO₂ concentration
5.2%vol%
Facility scope
EngineeringSargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration5.2% vol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages5
Compression inlet—
Compression discharge2,215 psia
Description
Calpine Texas CCUS Holdings LLC, with Electricore Inc., is conducting a FEED study for a modular post-combustion CO₂ capture system at the Deer Park Energy Center NGCC plant in Texas. Using Shell’s commercial-scale amine technology, the system will capture 95% of emissions—about 5 MTPA—while maintaining low energy use and fast reaction rates. The study will include business case, techno-economic, life cycle, environmental, and public policy analyses, including environmental justice and job creation impacts.