甲烷化
放热反应
材料科学
推流式反应器模型
核工程
工作温度
催化作用
连续搅拌釜式反应器
化学工程
环境科学
热力学
化学
工程类
有机化学
物理
作者
Thomas Stiegler,Katharina Meltzer,Alexander Tremel,Manfred Baldauf,Peter Wasserscheid,Jakob Albert
标识
DOI:10.1002/ente.201900047
摘要
Herein, the use of an additively manufactured rack‐type reactor for CO 2 methanation under dynamic operating conditions is proposed. In detail, CO 2 methanation using an additively manufactured structured reactor (catalyst: 2.5 wt% Ru/Al 2 O 3 /MgO) is reported. The dynamic operation is simulated by changing the reactant flow rates (loads) based on the operation strategy of an electrolyzer connected to a wind farm. Due to the high heat conductivity of the metallic structures, temperature hotspots related to load variations are avoided efficiently. In the test rig, these structured reaction systems reach equilibrium CO 2 ‐conversions with only minor axial temperature gradients for various loads and thus offer a high potential for the dynamic operation of exothermic gas‐phase processes.
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