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.
Peterhead Power Station (Aberdeenshire)
CO₂ captured
1,000,000t/yr
Capture efficiency
90.0%
Utilization
—
Parasitic load
—MW
CO₂ concentration
—
Facility scope
Engineering—
Point source approachPost-Combustion Capture
CO₂ concentration—
Flue gas pressure—
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge1,754 psia
Description
The Peterhead CCS Project in Aberdeenshire, Scotland, was designed to demonstrate the world’s first commercial-scale post-combustion CO₂ capture from a gas-fired power station. Using amine-based CANSOLV technology, it aimed to capture around one million tonnes of CO₂ annually from one turbine at SSE’s Peterhead Power Station, compress and condition it, and transport it via a new offshore pipeline for injection into the depleted Goldeneye gas reservoir over 2 km beneath the North Sea. The FEED study defined project scope, refined CAPEX and OPEX estimates, and assessed cost uncertainties, providing a basis for the Execute phase while also documenting budget performance and emergent costs during FEED.
Phillips 66 / Rodeo Refinery
CO₂ captured
190,000t/yr
Capture efficiency
95.0%
Utilization
94.5%
Parasitic load
—MW
CO₂ concentration
18.0%vol%
Facility scope
EngineeringWorley
Point source approachPre-Combustion Capture
CO₂ concentration18.0% vol%
Flue gas pressure20 psia
Compressor nameplate—
Compression stages5
Compression inlet25 psia
Compression discharge2,250 psia
Description
Phillips 66, with Worley Group Inc., is developing the initial design for a commercial-scale CCS system at the Rodeo Refinery hydrogen plant, targeting over 90% capture efficiency and storage of about 190,000 tonnes of CO₂ annually. The project will evaluate three capture configurations—flue gas plus PSA tail gas, syngas plus flue gas, and flue gas only—selecting the most cost-effective option through a techno-economic analysis. The chosen design will be advanced to a level suitable for the next engineering phase, concluding with a final TEA for the selected CCS configuration.
Southern Company / Plant Barry
CO₂ captured
1,632,000t/yr
Capture efficiency
95.0%
Utilization
85.0%
Parasitic load
18.4MW
CO₂ concentration
6.7%mol%
Facility scope
EngineeringLinde Engineering (process engineering and equipment cost), Kiewit (plant layout, constructability, installation)
Point source approachPost-Combustion Capture
CO₂ concentration6.7% mol%
Flue gas pressure14 psia
Compressor nameplate20.8 MW
Compression stages—
Compression inlet—
Compression discharge2,215 psia
Description
General Electric Gas Power, with Linde, Kiewit, and Southern Company Services, is conducting a FEED study for a “Generation 2” amine-based post-combustion CO₂ capture system at an existing NGCC power plant. Targeting at least 95% capture efficiency, the design will emphasize optimized integration, lower CCS costs, and flexible operation to complement renewable energy. The 18-month project will progress from multiple conceptual designs to a single configuration, culminating in a detailed design, technical viability assessment, techno-economic and life cycle analyses, and a business case evaluation.