A CO2 valorization plant to produce light hydrocarbons: Kinetic model, process design and life cycle assessment. (January 2023)

• Record Type: Journal Article
• Authors: Cordero-Lanzac, Tomás; Ramirez, Adrian; Cruz-Fernandez, Marta; Zander, Hans-Jörg; Joensen, Finn; Woolass, Steven; Meiswinkel, Andreas; Styring, Peter; Gascon, Jorge; Olsbye, Unni
• Is Part Of: Journal of CO₂ utilization. Volume 67(2023)
• Publication Date: 2023-01
• Subjects: Tandem catalyst -- Kinetics -- Reactor design -- Process modeling -- LCA; Carbon dioxide -- Periodicals; Carbon dioxide -- Environmental aspects -- Periodicals; Carbon dioxide mitigation -- Periodicals; Carbon dioxide; Carbon dioxide -- Environmental aspects; Carbon dioxide mitigation; Periodicals; 628.53205
• DOI: 10.1016/j.jcou.2022.102337
• Languages: English
• ISSNs: 2212-9820

Abstract

Abstract: Reliable Life Cycle Assessment (LCA) of processes for valorization of CO2 -rich off-gas streams requires multidisciplinary contributions that span the development of active and selective catalysts, reactor design, plant modeling and optimization, as well as environmental impact analysis. Herein, we present the design and study of a CO2 valorization plant through methanol-mediated (tandem) hydrogenation to light hydrocarbons, with propane as the most abundant product. A state-of-the-art PdZn/ZrO2 + SAPO-34 catalyst combination was screened for catalytic activity and selectivity in a wide operation range. Optimal process conditions were found at 350 °C, 30–40 bar and co-feeding of CO2 /CO. Kinetic parameters for the tandem reaction were extracted and used for the design of a multi-layer reactor, where the two catalysts are distributed according to: (i) CO2 -to-methanol catalyst; (ii) mixed catalyst bed, and; (iii) methanol-to-hydrocarbons catalyst. This configuration outperformed the conventional dual bed and mixed bed reactor configurations in terms of process design. A Life Cycle Assessment of the plant suggested that a substantial decrease in the global warming impact of propane production will be highly driven by using green hydrogen from either solar or wind sources, although the comparison with fossil-derived propane indicated already a reasonable improvement even when using grey hydrogen from natural gas. Highlights: CO2 hydrogenation was studied using a PdZn/ZrO2 +SAPO-34 catalyst under a broad range of conditions. A kinetic model for the methanol-mediated (tandem) CO2 -to-LPG was developed. A CO2 valorization plant to LGP was designed using an innovative three-layer reactor. Gate-to-gate LCA for propane production suggested environmental benefits of the CO2 valorization plant.