Valorization of refinery fuel gas and biogenic gases from thermochemical conversion into low-carbon methanol

By-product fuel gases from refinery operations are a major heat source in fossil refineries and their availability poses a challenge to the deployment of low-carbon heat sources. This study evaluates the valorization of refinery fuel gases (RFG) into low-carbon methanol via co-processing with residual biogenic gas streams from biomass thermochemical conversion. Results from techno-economic analysis indicate that up to 44 wt.% of biogenic blend is possible without the need for external hydrogen supply, while electricity and heat requirements per tonne of methanol change by -4 % and + 80% respectively. Nevertheless, at the 44 wt.% blend, the estimated methanol cost increases only by 2.4 % (0.43 EUR/kg), while the reduction in methanol carbon intensity is approximately 40 %. This highlights promising benefits that can contribute to the integration of bio-oils producing technologies within fossil refineries.

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Publication Details

Journal
Systems and Control Transactions
Published
2025-06-30
DOI
https://doi.org/10.69997/sct.173711
Primary Topic
Thermochemical Biomass Conversion Processes
Type
article
Field-Weighted Citation Impact
0.00

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article

Valorization of refinery fuel gas and biogenic gases from thermochemical conversion into low-carbon methanol

Andrea Ramírez, Eliana Lozano Sanchez, Erik López-Basto
Systems and Control Transactions
Thermochemical Biomass Conversion Processes
article

Valorization of refinery fuel gas and biogenic gases from thermochemical conversion into low-carbon methanol

Andrea Ramírez, Eliana Lozano Sanchez, Erik López-Basto
article en

Abstract

By-product fuel gases from refinery operations are a major heat source in fossil refineries and their availability poses a challenge to the deployment of low-carbon heat sources. This study evaluates the valorization of refinery fuel gases (RFG) into low-carbon methanol via co-processing with residual biogenic gas streams from biomass thermochemical conversion. Results from techno-economic analysis indicate that up to 44 wt.% of biogenic blend is possible without the need for external hydrogen supply, while electricity and heat requirements per tonne of methanol change by -4 % and + 80% respectively. Nevertheless, at the 44 wt.% blend, the estimated methanol cost increases only by 2.4 % (0.43 EUR/kg), while the reduction in methanol carbon intensity is approximately 40 %. This highlights promising benefits that can contribute to the integration of bio-oils producing technologies within fossil refineries.

Systems and Control TransactionsVol. 4
Ecopetrol (Colombia) (CO), Aalborg University (DK), Delft University of Technology (NL)
Villum Fonden
Openalex Percentile: Top 86%
Thermochemical Biomass Conversion Processes
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