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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.

Holcim / Ste. Genevieve Cement Plant

CementFEED· University of Illinois· 2024-08-29Project page ↗Cost report ↗
CO₂ captured
3,056,339t/yr
Capture efficiency
95.0%
Utilization
85.0%
Parasitic load
60MW
CO₂ concentration
20.3%mol%
Facility scope
EngineeringKiewit
Point source approachPost-Combustion Capture
CO₂ concentration20.3% mol%
Flue gas pressure16 psia
Compressor nameplate
Compression stages
Compression inlet
Compression discharge2,215 psia
Description
The University of Illinois at Urbana-Champaign is leading a FEED study for a commercial-scale CO₂ capture system at Holcim’s Ste. Genevieve cement plant in Missouri, targeting 95% capture efficiency. Using Air Liquide’s Cryocap™ technology, which combines PSA pre-concentration with cryogenic purification, the system will produce high-purity CO₂ for storage near the Prairie State Generating Company in Illinois. UIUC will manage the project and perform economic and impact analyses, while Air Liquide, Kiewit, Visage Energy, and Holcim will contribute to design, safety, environmental, and site integration efforts.

Rayburn Energy Station / Sherman Power Plant

Natural GasFEED· Bechtel· 2022-03-01Project page ↗Cost report ↗
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.

Nutrien Redwater Nitrogen Operations

AmmoniaFEED· Nutrien· 2024-11-01Project page ↗
CO₂ captured
747,155t/yr
Capture efficiency
95.0%
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
CO₂ capture from the SMR flue gas stacks located in Plant 01 and Plant 09 of the facility. Combined flue gases from each of the two sources would be collected and transported by ducts to the carbon capture facility. The design of the capture facility is 2,100 – 2,200 tpd of CO₂, including the CO₂ captured from the SMRs and additional flue gas generated from the steam boiler supplying the CCS unit. The CCS unit is to be designed for a minimum 30% plant turndown, this is to ensure the operation of CCS unit when flue gas from Plant 01 is the only feed to the CCS unit. For the purposes of the study the carbon capture facility design, including flue gas pretreatment and downstream CO₂ compression and dehydration, is provided by licensor. Hatch designed the flue gas transportation from the stacks to the Carbon Capture and Sequestration (CCS) unit battery limit, flue gas pressure boosting and Balance of Plant (BOP) which includes all the utility and offsite systems