| dc.contributor.author | Shin, Woojae | |
| dc.contributor.author | Lin, Bosong | |
| dc.contributor.author | Lai, Haoxiang | |
| dc.contributor.author | Ibrahima, Gasim | |
| dc.contributor.author | Zang, Guiyan | |
| dc.date.accessioned | 2026-02-26T16:10:15Z | |
| dc.date.available | 2026-02-26T16:10:15Z | |
| dc.date.issued | 2025-02-18 | |
| dc.date.submitted | 2024-09-10 | |
| dc.identifier.issn | 1463-9270 | |
| dc.identifier.uri | https://hdl.handle.net/1721.1/164965 | |
| dc.description.abstract | Ethylene, a building block of the chemical industry, significantly contributes to global greenhouse gas (GHG) emissions, prompting interest in decarbonization approaches to align with recent carbon neutrality initiatives. This paper presents a comprehensive techno-economic analysis (TEA) and life cycle analysis (LCA) of GHG emissions, comparing conventional ethane-based ethylene plants with three decarbonization approaches. The study was conducted within the context of the U.S. average, with sensitivity analysis to identify key drivers affecting well-to-gate (WTG) GHG emissions and the levelized cost of ethylene (LCOE). The conventional plant exhibited a GHG emission of 869 kgCO2e per tonne-ethylene and a LCOE of $746 per tonne-ethylene. Substituting external natural gas fuels with grid or renewable electricity decreased the emissions to 806 and 717 kgCO2e per tonne-ethylene, respectively. The emissions of the grid-powered or renewable-powered electrically heated cracker that exports co-produced hydrogen to substitute conventional gray hydrogen were 1031 and −163 kgCO2e per tonne-ethylene, respectively. The application of CCS to purge gas showed 703 and 514 kgCO2e per tonne-ethylene emissions, respectively. The electric cracker showed lower emissions than the conventional plant below 380 kgCO2e per MW h electricity upstream, and at 60 kgCO2e per MW h, it achieved carbon neutrality. Regarding LCOE, when using a grid electricity source, no external natural gas, electric cracker, and adding CCS to purge gas showed $743, 833, and 771 per tonne-ethylene, respectively. When these plants adopt renewable electricity, their LCOEs will be $737, 746 and 757 per tonne-ethylene. Below $41.1 per MW h electricity price, the electric cracker had the lowest value among all cases. With hydrogen prices of $0.5–3.0 per kg-H2, the electric cracker's LCOE ranged from −$45(cost)–128(saving) per tonne-ethylene compared to the conventional concept. | en_US |
| dc.publisher | Royal Society of Chemistry | en_US |
| dc.relation.isversionof | https://doi.org/10.1039/D4GC04538F | en_US |
| dc.rights | Creative Commons Attribution-Noncommercial | en_US |
| dc.rights.uri | https://creativecommons.org/licenses/by-nc/4.0/ | en_US |
| dc.source | Royal Society of Chemistry | en_US |
| dc.title | Decarbonization Approaches for Ethylene Production: Comparative Techno-Economic and Life-Cycle Analysis | en_US |
| dc.type | Article | en_US |
| dc.identifier.citation | Shin, Woojae, Lin, Bosong, Lai, Haoxiang, Ibrahima, Gasim and Zang, Guiyan. 2025. "Decarbonization Approaches for Ethylene Production: Comparative Techno-Economic and Life-Cycle Analysis." Green Chemistry, 27 (14). | |
| dc.contributor.department | MIT Energy Initiative | en_US |
| dc.relation.journal | Green Chemistry | en_US |
| dc.eprint.version | Final published version | en_US |
| dc.type.uri | http://purl.org/eprint/type/JournalArticle | en_US |
| eprint.status | http://purl.org/eprint/status/PeerReviewed | en_US |
| dspace.date.submission | 2026-02-13T16:40:15Z | |
| mit.journal.volume | 27 | en_US |
| mit.journal.issue | 14 | en_US |
| mit.license | PUBLISHER_CC | |
| mit.metadata.status | Authority Work and Publication Information Needed | en_US |