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.
Southern Company / Plant Daniel
CO₂ captured
1,769,520t/yr
Capture efficiency
90.0%
Utilization
—
Parasitic load
79MW
CO₂ concentration
—
Facility scope
EngineeringLinde Engineering (ISBL), Southern Company Services (OSBL)
Point source approachPost-Combustion Capture
CO₂ concentration—
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Southern Company Services, with Linde Gas North America, is conducting a FEED study for a commercial-scale CO₂ capture system using Linde-BASF’s advanced aqueous amine technology at an NGCC plant of at least 375 MWe. The project will evaluate Alabama Power’s Plant Barry and Mississippi Power’s Plant Daniel to select the optimal host site, define project requirements, optimize process design, and deliver engineering packages along with a cost and schedule estimate within 15% accuracy. The study will build on prior feasibility work and site-specific testing.
Linde / Port Arthur Facility
CO₂ captured
1,435,000t/yr
Capture efficiency
92.0%
Utilization
90.0%
Parasitic load
—MW
CO₂ concentration
16.2%mol%
Facility scope
EngineeringKiewit (EPC costs for Svante’s equipment, steam generators, and OSBL construction), Linde (EPC costs for CO₂ purification/compression and EP costs for OSBL utilities)
Point source approachPost-Combustion Capture
CO₂ concentration16.2% mol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Linde Inc., with Linde Engineering Americas, Linde Engineering Dresden, and Svante Inc., is completing an initial engineering design for a commercial-scale CO₂ capture plant at its steam methane reforming hydrogen facility in Port Arthur, Texas. Using Svante’s VeloxoTherm™ solid adsorbent technology, the system will capture about 1 million tonnes of CO₂ annually at ≥90% efficiency while producing 99.97% pure “blue” hydrogen. The design will include ISBL units for flue gas conditioning and CO₂ purification, OSBL components, and a techno-economic analysis of capture costs and hydrogen production economics.
Nutrien Redwater Nitrogen Operations
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