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.
Tampa Electric Polk Power Station Unit 2
CO₂ captured
3,420,780t/yr
Capture efficiency
95.0%
Utilization
—
Parasitic load
—MW
CO₂ concentration
4.5%vol%
Facility scope
EngineeringSargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration4.5% vol%
Flue gas pressure14 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Tampa Electric Company, with ION Clean Energy, Sargent & Lundy, Koch Specialty Plant Services, and Siemens Energy, completed a FEED study to retrofit post-combustion CO2 capture onto Unit 2 of the Polk Power Station, a 1,190 MWe (1,168 MWe net) 4x4x1 natural gas combined cycle plant in Mulberry, Florida. Using ION Clean Energy's ICE-31 advanced solvent across two parallel capture trains, the design targets at least 95% capture, nearly 3.7 million tonnes of CO2 per year, with downstream Siemens compression and dehydration and integrated pipeline transport to dedicated Class VI geologic storage. Each train includes a direct contact cooler, absorber, stripper, and compression, with the absorber columns sized to support 1x1 operation at 75% combustion turbine load to preserve dispatch flexibility. The study was funded under DOE Award DE-FE0032224 and produced an AACE Class 3 (-20%/+30%) capital cost and cost-of-capture estimate.
Linde Hydrogen Plant
CO₂ captured
1,360,000t/yr
Capture efficiency
95.0%
Utilization
—
Parasitic load
—MW
CO₂ concentration
18.3%mol%
Facility scope
EngineeringLinde Engineering
Point source approachPost-Combustion Capture
CO₂ concentration18.3% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Linde Inc., with Linde Engineering Americas and BASF, is conducting an initial engineering design for a 3,500 tonnes/day CO₂ capture plant using Linde-BASF’s advanced aqueous amine technology at a Linde-owned steam methane reforming facility. The project will define integration options, establish project requirements, optimize process design, and develop engineering, cost, and schedule packages. BASF will provide the technology design, LEA will deliver detailed engineering and constructability assessments, and Linde will lead techno-economic, environmental, and safety analyses in coordination with the SMR plant operators.
Gerald Gentleman Station
CO₂ captured
4,316,020t/yr
Capture efficiency
89.8%
Utilization
85.0%
Parasitic load
—MW
CO₂ concentration
—
Facility scope
EngineeringSargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration—
Flue gas pressure—
Compressor nameplate—
Compression stages6
Compression inlet—
Compression discharge2,115 psia
Description
ION Clean Energy, with Nebraska Public Power District, is conducting a FEED study to retrofit a CO₂ capture system on Unit 2 of the 700 MWe Gerald Gentleman Station in Nebraska. Using ION’s low-aqueous ICE-21 solvent, proven in prior DOE-funded projects to reduce energy use, solvent degradation, and emissions, the design will feature two parallel 350 MWe capture units. The project aims to decarbonize most of Unit 2 while maintaining maximum operational flexibility for the plant.