Year: 2025
Type: article
Abstract: Ethylene, a major building block in the chemical industry, is predominantly produced via steam cracking, a non-catalytic process where ethane (or naphtha) is mixed with steam and thermally dehydrogenated at ~850°C. While this process is commercially widely deployed, it faces significant challenges including coking of the reactor and large CO2 emissions due to the high-temperature operation and large steam co-feed. The present work evaluated the use of liquid metals as an alternate, robust reaction media to address these challenges. Using bismuth-based liquid metal systems, we demonstrate via a combination of experimental studies and kinetic simulations that pure bismuth exhibits minimal catalytic activity but functions as a highly effective, integrated coke separator that enables ethylene yields that exceed commercial steam cracking while entirely eliminating the need for steam. This results in more than 30% savings in process energy, enabling a reduction in global CO2 emissions from ethylene production by 39 million tons of CO2,eq per year. The unique robustness of this system against deactivation via coking is confirmed by intentionally increasing coke formation via alloying Bi with 5wt% Ni and demonstrating stable operation for at least 100 hours time-on-stream. This liquid NiBi system shows five orders of magnitude reduction in deactivation rate compared to a conventional solid 5 wt% Ni/SiO2 catalyst which deactivates within minutes. These results suggest new avenues for catalytic and non-catalytic ethane dehydrogenation and related reactions by exploiting the exceptional resilience of liquid metal systems in heavily coke-forming environments, lowering energy intensity and carbon footprint for hydrocarbon processing.
Source: Energy & Fuels
Authors: Aime Laurent Twizerimana, Aaditya Hari Bharanidharan, Kyle McGaughy, Kaylen Ocampo, Christopher Eliot Parker, Mohammad S. Masnadi, Götz Veser
Institution: University of Pittsburgh
Language: English
Subfield: Catalysis
Field: Chemical Engineering
Domain: Physical Sciences
Open Access status: hybrid
Estimated APC paid: $4,500
OpenAlex ID: W4409624950
