首页> 外文期刊>The Canadian Journal of Chemical Engineering >Synthesis Gas Production with Simultaneous CO2 Capturing and Consuming: Application of Chemical Looping Combustion by Employing Fe45-Al2O3 and Mn40/Mg-ZrO2 Oxygen Carriers
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Synthesis Gas Production with Simultaneous CO2 Capturing and Consuming: Application of Chemical Looping Combustion by Employing Fe45-Al2O3 and Mn40/Mg-ZrO2 Oxygen Carriers

机译:同时捕获和消耗二氧化碳的合成气生产:通过使用Fe45-Al2O3和Mn40 / Mg-ZrO2氧气载体在化学回路燃烧中的应用

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摘要

In this study, thermal coupling of chemical looping combustion (CLC) and dry reforming of methane (DR) via employment of Fe45-Al2O3 and Mn40/Mg-ZrO2 oxygen carriers (OCs) were investigated. The main aim of this configuration (CLC-DR) is the prevention of large CO2 emissions to the atmosphere by CLC and simultaneous consumption of the captured gas to synthesis gas through a DR reaction. For this purpose, a steady state one-dimensional heterogeneous catalytic reaction model is applied to analyze the performance and applicability of the proposed CLC-DR configuration using both OCs. Simulation results indicate that for both OCs, combustion efficiency reaches 1 in the fuel reactor (FR) of CLC-DR. Additionally, results illustrate that CH4 conversion in the DR side of CLC-DR reaches 0.7235 and 0.7213 with Fe45-Al2O3 and Mn40/Mg-ZrO2 OCs respectively.
机译:在这项研究中,通过使用Fe45-Al2O3和Mn40 / Mg-ZrO2氧载体(OCs)研究了化学循环燃烧(CLC)和甲烷的干重整(DR)的热耦合。这种配置(CLC-DR)的主要目的是防止通过CLC向大气排放大量CO2,并通过DR反应将捕获的气体同时消耗为合成气。为此,将稳态一维非均相催化反应模型应用于分析使用两种OC的拟议CLC-DR构型的性能和适用性。仿真结果表明,对于两种OC,CLC-DR的燃料反应堆(FR)的燃烧效率均达到1。此外,结果表明,使用Fe45-Al2O3和Mn40 / Mg-ZrO2 OCs,CLC-DR的DR侧的CH4转化率分别达到0.7235和0.7213。

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