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ION Engineering, LLC (ION), has teamed with Nebraska Public Power District (NPPD), Sargent & Lundy, LLC, and Koch Modular Process Systems to develop a detailed design and cost estimate for a commercial-scale (300 MWe) slipstream carbon dioxide (CO2) capture facility for NPPD’s Gerald Gentleman Station (GGS). The team will produce a comprehensive overview of the costs associated with retrofitting the GSS coal-fired power generating Unit 2 to use ION’s solvent-based capture process for removing CO2 from flue gas. ION’s water-lean solvent exhibits significant reductions in regeneration energy requirements and significantly higher CO2 loading capacities when compared with the commercially available and most widely used amine-based solvent, monoethanolamine (MEA). The solvent’s properties result in reduced parasitic loads, liquid solvent flow rates, corrosion, maintenance, and equipment sizes when scaled-up for commercial systems, leading to reductions in both capital and operating expenses. During a recent U.S. Department of Energy (DOE)-funded project, the advanced CO2capture solvent was tested at pilot scale (12 MWe) at the CO2 Technology Centre in Mongstad, Norway. The campaign included 2,750 hours of testing with capture of more than 14,000 tonnes of CO2 with greater than 98 percent purity, outperforming MEA with a greater than 30 percent energy savings. The team will include the following process improvements in the design for the GSS Unit 2: solvent split-stream integration, flue gas heat recovery, and water use minimization. In addition to the design of the capture system, a capital cost estimate, encompassing both engineering design and construction for the carbon capture process and balance of plant systems, and a techno-economic analysis will be prepared.

Predecessor Projects: FE0005799FE0013303

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Nebraska Public Power District Gerald Gentleman Station near Sutherland, Nebraska
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Principal Investigator
Alfred Brown
brown@ion-engineering.com
Project Benefits

This advanced solvent-based capture process requires a smaller physical plant and less energy, improves CO2 product quality, and has lower solvent degradation, emissions, and water usage than commercially available amine-based capture systems. A commercial-scale detailed design and cost estimate of this low-cost advanced sorbent technology with process improvements for an existing coal-fueled generating unit will reduce the energy and capital cost associated with post-combustion carbon capture and allow for competitive operation of our Nation's fossil-based power generation infrastructure.

Project ID
FE0031595