Alkane dehydrogenation in scalable and electrifiable carbon membrane reactor

Alkane dehydrogenation in scalable and electrifiable carbon membrane reactor
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DOI:
10.1016/j.xcrp.2023.101692
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发表时间:
2023-11
影响因子:
8.9
通讯作者:
Lu Liu;A. Bhowmick;Sichao Cheng;Borja Hernandez Blazquez;Ying Pan;Junyan Zhang;Yuan Zhang
Lu Liu;A. Bhowmick;Sichao Cheng;Borja Hernandez Blazquez;Ying Pan;Junyan Zhang;Yuan Zhang
中科院分区:
综合性期刊2区
文献类型:
--
作者:
Lu Liu;A. Bhowmick;Sichao Cheng;Borja Hernandez Blazquez;Ying Pan;Junyan Zhang;Yuan Zhang

文献摘要

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Non-oxidative alkane dehydrogenation produces alkene and hydrogen products. The current processes face three challenges: limited conversion due to thermodynamics, rapid catalyst deactivation, and CO2emissions from process heating. A membrane reactor (MR) has the potential to overcome the thermodynamic limit by removing H2in situ, but both catalyst and membrane tend to deactivate quickly. Here, we report a carbon membrane reactor that integrates H2-permeable carbon molecular sieve (CMS) hollow fiber membranes and siliceous zeolite-supported metal catalysts. By lowering the reaction temperature using catalysts with a low threshold temperature and by overcoming the thermodynamic limit with CMS membranes, we achieve high conversion and catalyst stability. The electro-conductive nature of the CMS membrane enables joule heating of the reaction, reducing CO2emissions. We demonstrate a CMS membrane reactor with record-high stability for propylene and ethylene production, the second- and first-largest-volume chemicals used as feedstock globally.