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.
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.
Prairie State Generating
CO₂ captured
7,676,700t/yr
Capture efficiency
95.0%
Utilization
90.0%
Parasitic load
—MW
CO₂ concentration
11.4%vol%
Facility scope
EngineeringKiewit, Sargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration11.4% vol%
Flue gas pressure15 psia
Compressor nameplate—
Compression stages—
Compression inlet—
Compression discharge—
Description
Prairie State Generating Company is conducting a FEED study for a carbon capture facility on its 816 MWe Unit #2 in Illinois, using Mitsubishi Heavy Industries’ KM CDR Process™ with KS-21™ solvent. Designed to treat all flue gas from the unit, it would be the world’s largest post-combustion capture plant, compressing CO₂ for off-site sequestration. The project will leverage engineering support from Kiewit, Sargent & Lundy, and MHI.
Nutrien Redwater Nitrogen Operations
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.