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Title: Direct Conversion of Ethane to Oxygenates, Ethylene, and Hydrogen in a Noncatalytic Biphasic Plasma Microreactor

Journal Article · · ACS Sustainable Chemistry & Engineering

We selectively upgrade ethane (C2H6) to ethanol (C2H5OH), methanol (CH3OH), and acetic acid (CH3COOH) in a catalyst-free, continuous, argon/water biphasic plasma microreactor. The water (H2O) evaporates and electron- dissociates into OH· radicals. OH· recombines with alkyl radicals, produced via electron dissociation of ethane, to generate the oxygenates that absorb into H2O. A plasma-assisted path, reminiscent of the low-temperature thermocatalytic ethane steam reforming, leads to significant H2 coproduction. The gaseous stream also comprises CO2 and C2H4. Up to 1.3 and 1 μmol min–1 of liquid C2H5OH and CH3OH are attained, respectively. Compared to CO2-assisted ethane plasma conversion, which produces many oxygenates with low selectivity, the carbon selectivity can range from >70% C2H5OH, CH3OH, and CH3COOH to 60% C2H4. Furthermore, the low carbon footprint, electrified, modular, intensified process using a reactive evaporation and separation plasma could pave the way for the valorization of underutilized shale gas resources in remote areas.

Research Organization:
RAPID Manufacturing Institute, New York, NY (United States)
Sponsoring Organization:
USDOE Office of Energy Efficiency and Renewable Energy (EERE), Energy Efficiency Office. Advanced Materials & Manufacturing Technologies Office (AMMTO)
Grant/Contract Number:
EE0007888
OSTI ID:
2007401
Journal Information:
ACS Sustainable Chemistry & Engineering, Vol. 11, Issue 21; ISSN 2168-0485
Publisher:
American Chemical Society (ACS)Copyright Statement
Country of Publication:
United States
Language:
English

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Figures / Tables (4)