Field-Scale Testing of a High-Efficiency Membrane Reactor (MR)—Adsorptive Reactor (AR) Process for H<sub>2</sub> Generation and Pre-Combustion CO<sub>2</sub> Capture
Nicholas Margull,
Doug Parsley,
Ibubeleye Somiari,
Linghao Zhao,
Mingyuan Cao,
Dimitrios Koumoulis,
Paul K. T. Liu,
Vasilios I. Manousiouthakis,
Theodore T. Tsotsis
Affiliations
Nicholas Margull
Chemical and Biomolecular Engineering Department, University of California, Los Angeles, CA 90095, USA
Doug Parsley
Media and Process Technology, Inc., Pittsburgh, PA 15328, USA
Ibubeleye Somiari
Chemical and Biomolecular Engineering Department, University of California, Los Angeles, CA 90095, USA
Linghao Zhao
Mork Family Department of Chemical Engineering and Materials Science, University of Southern California, University Park, Los Angeles, CA 90089, USA
Mingyuan Cao
Mork Family Department of Chemical Engineering and Materials Science, University of Southern California, University Park, Los Angeles, CA 90089, USA
Dimitrios Koumoulis
Institute for Decarbonization and Energy Advancement, University of Kentucky, Lexington, KY 40507, USA
Paul K. T. Liu
Media and Process Technology, Inc., Pittsburgh, PA 15328, USA
Vasilios I. Manousiouthakis
Chemical and Biomolecular Engineering Department, University of California, Los Angeles, CA 90095, USA
Theodore T. Tsotsis
Mork Family Department of Chemical Engineering and Materials Science, University of Southern California, University Park, Los Angeles, CA 90089, USA
The study objective was to field-validate the technical feasibility of a membrane- and adsorption-enhanced water gas shift reaction process employing a carbon molecular sieve membrane (CMSM)-based membrane reactor (MR) followed by an adsorptive reactor (AR) for pre-combustion CO2 capture. The project was carried out in two different phases. In Phase I, the field-scale experimental MR-AR system was designed and constructed, the membranes, and adsorbents were prepared, and the unit was tested with simulated syngas to validate functionality. In Phase II, the unit was installed at the test site, field-tested using real syngas, and a technoeconomic analysis (TEA) of the technology was completed. All project milestones were met. Specifically, (i) high-performance CMSMs were prepared meeting the target H2 permeance (>1 m3/(m2.hbar) and H2/CO selectivity of >80 at temperatures of up to 300 °C and pressures of up to 25 bar with a 2.5 wt.% and an attrition rate of 2 capture goals of 95% CO2 purity at a cost of electricity (COE) 30% less than baseline approaches.
