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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.

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Comparing 3 reports — tab selection applies to every column.

Nutrien Redwater Nitrogen Operations

AmmoniaFEED· Nutrien· 2024-11-01Project page ↗
CO₂ captured
683,645t/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
Scope starts with the receipt of natural gas and fuel gas mixture from the existing Plant 01 and Plant 09 source and terminates with hydrogen (H₂) at the required specification and conditions to be used as fuel in the existing SMR unit. High concentration CO₂ from the ATR is captured and H₂ production from the proposed facility will replace the fuel gas feed to the primary reformer for heating. The facility capacity is based on the heating duty required to replace the current fuel source. The scope for the study involves the new ATR unit and associated downstream shift, CO₂ capture, and syngas purification unit. The project scope also includes an ASU to supply oxygen to the ATR unit.

Finnish Market Pulp Mill / Capture of CO2 in both Kraft & Multi-boilers

Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
1,749,600t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
28.5MW
CO₂ concentration
15.0%mol%
Facility scope
Engineering
Point source approachPost-Combustion Capture
CO₂ concentration15.0% 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 both Kraft & Multi-boilers

Milton R. Young Power Plant

CoalFEED· Minnkota Power Cooperative· 2023-02-20Project page ↗Cost report ↗
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.