Non-Oxidative Coupling of Methane via Plasma-Catalysis Over M/γ-Al2O3 Catalysts (M = Ni, Fe, Rh, Pt and Pd): Impact of Active Metal and Noble Gas Co-Feeding

被引:0
|
作者
Kechagiopoulos, Panagiotis N. [1 ]
Rogers, James [1 ]
Maitre, Pierre-Andre [1 ]
Mccue, Alan J. [2 ]
Bannerman, Marcus N. [1 ]
机构
[1] Univ Aberdeen, Sch Engn, Chem Proc & Mat Grp, Aberdeen AB24 3UE, Scotland
[2] Univ Aberdeen, Adv Ctr Energy & Sustainabil ACES, Sch Nat & Comp Sci, Dept Chem, Aberdeen AB24 3UE, Scotland
关键词
Plasma catalysis; Non-oxidative coupling; Methane; Argon; Helium; DIELECTRIC BARRIER DISCHARGE; INDUCED DISSOCIATIVE CHEMISORPTION; NONEQUILIBRIUM PLASMA; HYDROGEN-PRODUCTION; HIGHER HYDROCARBONS; NATURAL-GAS; CONVERSION; ACTIVATION; IGNITION; REACTOR;
D O I
10.1007/s11090-024-10507-2
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Plasma-catalysis has attracted significant interest in recent years as an alternative for the direct upgrading of methane into higher-value products. Plasma-catalysis systems can enable the electrification of chemical processes; however, they are highly complex with many previous studies even reporting negative impacts on methane conversion. The present work focuses on the non-oxidative plasma-catalysis of pure methane in a Dielectric Barrier Discharge (DBD) reactor at atmospheric pressure and with no external heating. A range of transition and noble metals (Ni, Fe, Rh, Pt, Pd) supported on gamma-Al2O3 are studied, complemented by plasma-only and support-only experiments. All reactor packings are investigated either with pure methane or co-feeding of helium or argon to assess the role of noble gases in enhancing methane activation via energy transfer mechanisms. Electrical diagnostics and charge characteristics from Lissajous plots, and electron temperature and collision rates calculations via BOLSIG+ are used to support the findings with the aim of elucidating the impact of both active metal and noble gas on the reaction pathways and activity. The optimal combination of Pd catalyst and Ar co-feeding achieves a substantial improvement over non-catalytic pure methane results, with C2+ yield rising from 30% to almost 45% at a concurrent reduction of energy cost from 2.4 to 1.7 MJmol(CH4)(-1) and from 9 to 4.7 MJmol(C2+)(-1). Pd, along with Pt, further displayed the lowest coke deposition rates among all packings with overall stable product composition during testing.
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页码:2057 / 2085
页数:29
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