催化作用
吸热过程
水煤气变换反应
产量(工程)
放热反应
化学工程
热力学平衡
多相催化
化学平衡
材料科学
化学
感应加热
相(物质)
化学反应
磁选
热力学
纳米颗粒
气相
过渡金属
相变
无机化学
磁性纳米粒子
化学反应器
温度梯度
水煤气
作者
Junhui Hu,Lise‐Marie Lacroix,Jacob Johny,Sourav Ghosh,Elisabeth Hannah Wolf,Jeongmin Ji,Sheng‐Hsiang Lin,Manisha Durai,Alin Benice Schöne,Walid Hetaba,Holger Ruland,Walter Leitner,Alexis Bordet
标识
DOI:10.1002/anie.202523576
摘要
Equilibrium-limited endothermic reactions play a crucial role in the transition toward a more sustainable chemical industry, but are typically plagued by the need for high operation temperatures (>500°C). Here, we show that the temperature gradients generated by the selective and localized heating of catalyst materials in a colder reactor environment shift the equilibrium of thermodynamically-limited endothermic reactions and improve their performance. In particular, the reverse water gas shift reaction and magnetic induction are selected as the model reaction and selective catalyst heating method, respectively. Magnetically induced catalysis using standard Cu-Al spinel-derived catalyst functionalized with carbon-coated iron nanoparticles enables high CO yield (up to 62%) at mild catalyst and reactor temperatures (estimated at 300°C and determined as 25-123°C, respectively). We demonstrate that the catalyst temperature and not the reactor temperature governs the equilibrium product composition of the rWGS, and that the temperature gradient promotes the in situ removal of water to shift the gas phase thermodynamic equilibrium. These two points synergistically result in a CO yield that would require a reactor temperature of 650°C in a conventionally heated gas phase reaction.
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