Back to Top
Skip to main content
NETL Logo

Ohio State University (OSU) will develop a cost-effective design and fabrication process for a novel amine-containing transformational membrane to capture carbon dioxide (CO2) from coal-derived syngas. The membrane consists of a CO2-selective and permeable layer on top of a nanoporous polymer support and exhibits chemical stability to hydrogen sulfide (H2S) gas. The membrane operates based on the facilitated transport mechanism, in which CO2 transfer through the membrane is enhanced via reaction with amino groups, while hydrogen (H2) is rejected due to the absence of reaction. Hydrogen sulfide can permeate through the membrane significantly faster than CO2 and can be removed in the front section of the membrane module, resulting in less than 30 ppm H2S in the retentate. The membrane will be used in a single-stage membrane process utilizing modules in commercial spiral-wound configuration with a minimal pressure drop. OSU will synthesize and characterize transformational membranes, scale up the best performing membrane using a continuous roll-to-roll fabrication method, and fabricate at least nine prototype membrane modules with an approximate membrane area of 800 cm2. Parametric testing of the membrane modules at 20-32 bar and 100-120°C will be performed to identify conditions for continuous steady-state operation, which will be conducted using simulated syngas at OSU for at least 200 hours. The membrane test data will be used to complete a high-level techno-economic analysis (TEA) and finalize the state point data table. American Electric Power will provide consulting support on the TEA and Microdyn-Nadir US Inc. will provide consultation on membrane scale-up and module fabrication.

image_plp
Single-stage membrane process
plp_DOD_share
Off
Presentations_plp
Principal Investigator
W. S. Winston Ho
ho.192@osu.edu
Project Benefits

The simplicity of the transformational membrane structure lowers its manufacturing cost. Optimization and scale up of transformational membranes with high CO2/H2 selectivity and CO2 permeance, along with testing of commercial spiral-wound membrane modules using simulated syngas, will make progress toward achieving CO2 capture with at least 95 percent CO2 purity at a cost of electricity 30 percent less than baseline capture approaches.

Project ID
FE0031635
Website
Ohio State University
https://www.osu.edu/