制氢
甲烷转化炉
甲烷
催化作用
电气化
工艺工程
蒸汽重整
氢
反应堆设计
核工程
比例(比率)
废物管理
环境科学
生产(经济)
化学
电
工程类
电气工程
物理
经济
有机化学
宏观经济学
量子力学
生物化学
作者
Sebastian T. Wismann,Jakob S. Engbæk,Søren B. Vendelbo,Flemming Buus Bendixen,Winnie L. Eriksen,Kim Aasberg‐Petersen,Cathrine Frandsen,Ib Chorkendorff,Peter Mortensen
出处
期刊:Science
[American Association for the Advancement of Science (AAAS)]
日期:2019-05-23
卷期号:364 (6442): 756-759
被引量:401
标识
DOI:10.1126/science.aaw8775
摘要
Electrification of conventionally fired chemical reactors has the potential to reduce CO2 emissions and provide flexible and compact heat generation. Here, we describe a disruptive approach to a fundamental process by integrating an electrically heated catalytic structure directly into a steam-methane-reforming (SMR) reactor for hydrogen production. Intimate contact between the electric heat source and the reaction site drives the reaction close to thermal equilibrium, increases catalyst utilization, and limits unwanted byproduct formation. The integrated design with small characteristic length scales allows compact reactor designs, potentially 100 times smaller than current reformer platforms. Electrification of SMR offers a strong platform for new reactor design, scale, and implementation opportunities. Implemented on a global scale, this could correspond to a reduction of nearly 1% of all CO2 emissions.
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