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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.

3 of 3 selectedClear selection46 reports
Comparing 3 reports — tab selection applies to every column.

Calpine / Deer Park Energy Center

Natural GasFEED· Calpine· 2024-05-30Project page ↗Cost report ↗
CO₂ captured
6,200,000t/yr
Capture efficiency
95.0%
Utilization
90.0%
Parasitic load
184MW
CO₂ concentration
5.2%vol%
Facility scope
EngineeringSargent & Lundy
Point source approachPost-Combustion Capture
CO₂ concentration5.2% vol%
Flue gas pressure15 psia
Compressor nameplate
Compression stages8
Compression inlet
Compression discharge2,215 psia
Description
Calpine Texas CCUS Holdings LLC, with Electricore Inc., is conducting a FEED study for a modular post-combustion CO₂ capture system at the Deer Park Energy Center NGCC plant in Texas. Using Shell’s commercial-scale amine technology, the system will capture 95% of emissions—about 5 MTPA—while maintaining low energy use and fast reaction rates. The study will include business case, techno-economic, life cycle, environmental, and public policy analyses, including environmental justice and job creation impacts.

Finnish Market Pulp Mill / Capture of CO2 in Kraft, Multi-fuel Boilers & Lime Kiln

Pulp and Paperpre-FEED· VTT Technical Research Centre of Finland· 2016-12-01Project page ↗Cost report ↗
CO₂ captured
1,946,575t/yr
Capture efficiency
90.0%
Utilization
95.9%
Parasitic load
31.4MW
CO₂ concentration
15.7%mol%
Facility scope
Engineering
Point source approachPost-Combustion Capture
CO₂ concentration15.7% mol%
Flue gas pressure
Compressor nameplate
Compression stages4
Compression inlet
Compression discharge1,595 psia
Description
Analysis sets the design and cost-estimating basis for evaluating pulp and board mills with and without CCS. Two base cases are considered: a market pulp mill and an integrated pulp and board mill. Six CCS cases are evaluated, capturing CO₂ from the recovery boiler, multi-fuel boiler, lime kiln, or their combinations. The mills are assumed to be energy independent, with black liquor and bark burned to produce steam and electricity, and excess electricity exported to the grid. The CO₂ capture system uses post-combustion MEA technology with a 90% capture rate, and if on-site electricity is insufficient, an auxiliary boiler firing forest residues will supply the additional energy. Capture of CO2 in Kraft, Multi-fuel Boilers & Lime Kiln

Gerald Gentleman Station

CoalFEED· ION Clean Energy· 2023-03-01Project page ↗Cost report ↗
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.