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.
Milton R. Young Power Plant
CO₂ captured
4,297,145t/yr
Capture efficiency
90.0%
Utilization
85.0%
Parasitic load
83.3MW
CO₂ concentration
8.6%vol%
Facility scope
EngineeringFluor
Point source approachPost-Combustion Capture
CO₂ concentration8.6% vol%
Flue gas pressure—
Compressor nameplate44.4 MW
Compression stages—
Compression inlet—
Compression discharge1,690 psia
Description
Milton R. Young Station Unit 2 is conducting a FEED study to add a post-combustion CO₂ capture system using Fluor’s Econamine FG Plus™ technology to its lignite-fueled power plant in North Dakota. The design targets 3.6 million tonnes of CO₂ captured annually—twice the scale of the largest existing facility—while integrating advanced heat recovery, aerosol and solvent degradation controls, and cold-climate optimization to achieve the lowest levelized cost of capture at world scale. The study will deliver detailed design, cost, and performance data for financing, permitting, and final project scheduling.
Finnish Market Pulp Mill / Capture of CO2 in the Lime Kiln only
Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
197,008t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
2.8MW
CO₂ concentration
27.6%mol%
Facility scope
Engineering—
Point source approachPost-Combustion Capture
CO₂ concentration27.6% 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 Lime Kiln only
Rayburn Energy Station / Sherman Power Plant
CO₂ captured
645,000t/yr
Capture efficiency
85.0%
Utilization
57.0%
Parasitic load
67.3MW
CO₂ concentration
6.0%mol%
Facility scope
EngineeringBechtel
Point source approachPost-Combustion Capture
CO₂ concentration6.0% mol%
Flue gas pressure—
Compressor nameplate—
Compression stages4
Compression inlet—
Compression discharge2,190 psia
Description
Bechtel National Inc., with the Electric Power Research Institute, is conducting a FEED study to retrofit Panda Power Funds’ 758 MWe natural gas combined cycle plant in Sherman, Texas, with a post-combustion CO₂ capture system. Using an open-access design and a conventional amine absorber-stripper system with a non-proprietary solvent such as MEA, the project targets CO₂ capture for enhanced oil recovery.