Nonoxidative coupling of methane to olefins and aromatics over molten W-In bimetal catalyst

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Abstract

Direct nonoxidative conversion of methane to ethylene, aromatics and hydrogen has been recognized as an attractive utilization of natural gas, but qualified catalyst faces huge challenges. Most catalysts reported for this reaction are deactivated fast by carbon deposition. Herein, we demonstrated an active, selective and stable molten tungsten-indium bimetal catalyst entrapped in a silica gel, offering 11% methane conversion in single pass, with C2/C3-C5/aromatics hydrocarbon distributions of 36%/4%/54% at 950 °C. A little carbon was formed during reaction, but spontaneously floated onto tungsten-indium liquid surface and moved onto silica surface thereby leaving the tungsten-indium liquid surface clean. No deactivation was thus observed even after 120-hour testing. Theoretical calculations and experimental results reveal that methane is converted into ethane on indium clusters, followed by gas-phase thermal cracking to ethylene and tandem aromatization on tungsten clusters to aromatics. The high stability and controllable hydrocarbon distribution promise our catalyst great potential of practical applications.

Original languageEnglish
Article number123333
JournalFuel
Volume316
DOIs
StatePublished - 15 May 2022

Keywords

  • Coke resistance
  • In
  • Molten metal catalyst
  • Nonoxidative coupling of methane
  • Theoretical calculations
  • W

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