Evaluating the techno-economic potential of defossilized air-to-syngas pathways

Journal Article (2023)
Author(s)

Hussain M. Almajed (University of Colorado Boulder)

Omar J. Guerra (National Renewable Energy Laboratory)

W. A. Smith (National Renewable Energy Laboratory, University of Colorado Boulder, TU Delft - ChemE/Materials for Energy Conversion and Storage)

Bri Mathias S. Hodge (University of Colorado Boulder, National Renewable Energy Laboratory)

Ana Somoza-Tornos (TU Delft - ChemE/Product and Process Engineering, University of Colorado Boulder)

Research Group
ChemE/Materials for Energy Conversion and Storage
Copyright
© 2023 Hussain M. Almajed, Omar J. Guerra, W.A. Smith, Bri Mathias Hodge, A. Somoza Tornos
DOI related publication
https://doi.org/10.1039/D3EE02589F
More Info
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Publication Year
2023
Language
English
Copyright
© 2023 Hussain M. Almajed, Omar J. Guerra, W.A. Smith, Bri Mathias Hodge, A. Somoza Tornos
Research Group
ChemE/Materials for Energy Conversion and Storage
Issue number
12
Volume number
16
Pages (from-to)
6127-6146
Reuse Rights

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Abstract

Defossilizing the chemical industry using air-to-chemical processes offers a promising solution to driving down the emission trajectory to net-zero by 2050. Syngas is a key intermediate in the chemical industry, which can be produced from electrolytic H2 and air-sourced CO2. To techno-economically assess possible emerging air-to-syngas routes, we develop detailed process simulations of direct air CO2 capture, proton exchange membrane water electrolysis, and CO2 electrolysis. Our results show that renewable electricity prices of ≤$15 per MW h enable the replacement of current syngas production methods with CO2 electrolysis at CO2 avoidance costs of about $200 per t-CO2. In addition, we identify necessary future advances that enable economic competition of CO2 electrolysis with traditional syngas production methods, including a reverse water gas shift. Indeed, we find an improved CO2 electrolysis process (total current density = 1.5 A cm−2, CO2 single-pass conversion = 54%, and CO faradaic efficiency = 90%) that can economically compete with the reverse water gas shift at an optimal cell voltage of about 2.00 V, an electricity price of $28–42 per MW h, a CO2 capture cost of $100 per t-CO2, and CO2 taxes of $100–300 per t-CO2. Finally, we discuss the integration of the presented emerging air-to-syngas routes with variable renewable power systems and their social impacts in future deployments. This work paints a holistic picture of the targets required to economically realize a defossilized syngas production method that is in alignment with net-zero goals.