Co-production of ethylene and hydrogen via oxidative coupling of methane: Improving techno-economics and sustainability under emerging hydrogen markets

This study proposes an integrated oxidative coupling of methane (OCM) process for the co-production of ethylene and hydrogen, aiming to overcome the limitations of conventional single-reactor OCM and improve system-level performance while addressing resource sustainability in ethylene production. The proposed processes employ a two-stage isothermal reaction system to improve methane conversion and C 2 selectivity, combined with an alternative separation strategy and on-site energy recovery via combined heat and power integration. Rigorous process simulations were conducted to establish mass and energy balances, followed by comprehensive techno-economic and environmental analysis. The optimal configuration achieved an ethylene unit production cost of 0.97 USD/kg, representing a 55.9% reduction relative to a conventional single-reactor OCM benchmark (2.2 USD/kg), driven by staged conversion, elimination of methane recycles, and hydrogen coproduction. Net CO 2 -equivalent emissions were reduced by 66.2% to 4.50 kg CO 2 per kg C 2 H 4 . Sensitivity analysis identified hydrogen value, methane price, and the methane/oxygen ratio as key determinants of economic feasibility. A multi-metric assessment incorporating energy use, carbon efficiency, feedstock availability, and price elasticity shows that methane-based direct conversion pathways exhibit favorable structural characteristics, particularly in terms of feedstock robustness. These results provide practical solutions to cost-competitively diversify resources for ethylene production, while leveraging emerging hydrogen markets. • Two-stage OCM reactors improve methane conversion and ethylene selectivity. • A developed process enables co-production of ethylene and hydrogen. • Ethylene unit production cost reaches 0.97 $/kg, 55.9% lower than benchmark. • Net CO 2-eq emissions reduced to 4.50 kg CO 2 per kg of ethylene, 66.2% improvement. • Multi-metric assessment supports methane-based routes for sustainable ethylene production.

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Publication Details

Journal
Resources Environment and Sustainability
Published
2026-03-01
DOI
https://doi.org/10.1016/j.resenv.2026.100332
Primary Topic
Catalysis and Oxidation Reactions
Type
article
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article

Co-production of ethylene and hydrogen via oxidative coupling of methane: Improving techno-economics and sustainability under emerging hydrogen markets

Jiyong Kim, Hegwon Chung, Yong Tae Kim, Thai Ngan Do
Resources Environment and Sustainability
Catalysis and Oxidation Reactions
article

Co-production of ethylene and hydrogen via oxidative coupling of methane: Improving techno-economics and sustainability under emerging hydrogen markets

Jiyong Kim, Hegwon Chung, Yong Tae Kim, Thai Ngan Do
article en

Abstract

This study proposes an integrated oxidative coupling of methane (OCM) process for the co-production of ethylene and hydrogen, aiming to overcome the limitations of conventional single-reactor OCM and improve system-level performance while addressing resource sustainability in ethylene production. The proposed processes employ a two-stage isothermal reaction system to improve methane conversion and C 2 selectivity, combined with an alternative separation strategy and on-site energy recovery via combined heat and power integration. Rigorous process simulations were conducted to establish mass and energy balances, followed by comprehensive techno-economic and environmental analysis. The optimal configuration achieved an ethylene unit production cost of 0.97 USD/kg, representing a 55.9% reduction relative to a conventional single-reactor OCM benchmark (2.2 USD/kg), driven by staged conversion, elimination of methane recycles, and hydrogen coproduction. Net CO 2 -equivalent emissions were reduced by 66.2% to 4.50 kg CO 2 per kg C 2 H 4 . Sensitivity analysis identified hydrogen value, methane price, and the methane/oxygen ratio as key determinants of economic feasibility. A multi-metric assessment incorporating energy use, carbon efficiency, feedstock availability, and price elasticity shows that methane-based direct conversion pathways exhibit favorable structural characteristics, particularly in terms of feedstock robustness. These results provide practical solutions to cost-competitively diversify resources for ethylene production, while leveraging emerging hydrogen markets. • Two-stage OCM reactors improve methane conversion and ethylene selectivity. • A developed process enables co-production of ethylene and hydrogen. • Ethylene unit production cost reaches 0.97 $/kg, 55.9% lower than benchmark. • Net CO 2-eq emissions reduced to 4.50 kg CO 2 per kg of ethylene, 66.2% improvement. • Multi-metric assessment supports methane-based routes for sustainable ethylene production.

Resources Environment and Sustainability
Argonne National Laboratory (US), Korea Research Institute of Chemical Technology (KR), Sungkyunkwan University (KR)
Industry, innovation and infrastructure
Openalex Percentile: Top 9%
Catalysis and Oxidation Reactions
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