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Materials Today Chemistry · 2022 · IF 7.613

Combining electrolysis with thermocatalysis for dry reforming of methane in a naturally stratifying liquid alloy-salt catalytic system

Q. Yang,J. Liu,C. Zhou,J. Ni,E.I. Vovk,Y. Yang,B. Yang,X. Guan

Dry reforming of methane (CH 4 ) with carbon dioxide (CO 2 ) is an attractive technology for producing value-added syngas and mitigating greenhouse gas emission. However, this process usually requires high energy input due to the intrinsic inertness of CH 4 and CO 2 . Besides, the widely investigated solid Ni-based catalysts typically suffer from coking and sintering issues, leading to degradation in catalytic performance. Liquid alloys and molten salts are emerging as promising catalytic materials for CH 4 dry reforming. In this work, we combine electrolysis with thermocatalysis for CH 4 dry reforming in a naturally stratifying liquid alloy-salt system, which achieves effective and stable catalytic performance under relatively mild operation conditions. The conversions of CH 4 and CO 2 reach 37% and 95%, respectively, in a bubble column reactor comprising Ni–Bi alloy and LiNaCO 3 during constant current electrolysis at 1.5 A and 900 °C. The selectivities of H 2 and CO were maintained at 85% and 92%, respectively. Ab initio molecular dynamics simulation shows that the oxides of both Ni and Bi promote the C–H bond dissociation. Therefore, the electrochemical process combine electrolysis with thermocatalysis in the liquid alloy-salt system represents a promising approach to achieving effective and stable CH 4 dry reforming.

CAS / MDL: 7440-02-0
研究领域: 化学工程 · 催化 · 能源科学 · 环境科学
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Sustainable Energy & Fuels · 2020 ·Vol. 4 ·期 6 ·2768-2774 · IF 5.503

Methane dry reforming in a coking- and sintering-free liquid alloy-salt catalytic system

Qinghai Yang,Congquan Zhou,Jihong Ni,Xiaofei Guan

We present a liquid catalytic system comprising a liquid Ni–Bi alloy and a molten K2CO3 salt, which completely resolves the coking and sintering issues for dry reforming. The conversions of CH4 and CO2 reach 60% and 70%, respectively, in a 30 cm bubble column comprising 15 cm Ni0.27Bi0.73 and 15 cm K2CO3 at 1050 °C. The CO selectivity is near 100% throughout the temperature range of 950–1050 °C. A 120 hour stability test at 1000 °C shows no performance degradation, suggesting a stable and effective dry reforming process for syngas production. The catalytic performance and durability demonstrated highlight the potential of dry reforming for commercial applications.

CAS / MDL: 7440-02-0
研究领域: 化学工程 · 催化 · 能源转换
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