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Novel method for investigation of a K-Mg-based CO2 sorbent for sorption-enhanced water-gas shift reaction

机译:研究用于增强吸附的水煤气变换反应的K-Mg基CO2吸附剂的新方法

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摘要

CO2 sorption reactions at 20 bar and two different temperatures (i.e., 180 and 220 degrees C) using a K-Mg-based CO2 sorbent were carried out in a custom-designed high-pressure thermogravimetric analyzer (pressurized bubbling fluidized bed reactor on a scale) coupled with a gas chromatograph. The experimental apparatus, including the thermogravimetric analyzer, was custom-designed to measure weight changes caused by either CO2 sorption or water sorption or both. Analysis of the CO2 sorption reaction revealed that water sorption takes place rapidly with a moderate CO2 sorption rate at the early stage of the reaction. Then, the reaction migrates to CO2 sorption with simultaneous water desorption. Therefore, the mechanism of the CO2 sorption reaction is assumed to consist of fast hydration of K2CO3 and MgO, formation and decomposition of KHCO3, and finally carbonation of Mg(OH)(2) resulting in MgCO3 as the main product. K2CO3 is assumed to provide an efficient pathway for CO2 and water to travel into the core region of the sorbent via a reversible reaction between K2CO3 and KHCO3. (C) 2015 Elsevier Ltd. All rights reserved.
机译:在基于K-Mg的CO2吸附剂下,在20 bar和两个不同温度(即180和220摄氏度)下进行的CO2吸附反应在定制设计的高压热重分析仪(加压鼓泡流化床反应器规模)结合气相色谱仪。包括热重分析仪在内的实验设备是定制设计的,用于测量由CO2吸附或水吸附或两者引起的重量变化。对CO2吸附反应的分析表明,在反应的早期,水吸附迅速发生,并且具有中等的CO2吸附速率。然后,反应迁移至CO2吸附,同时发生水脱附。因此,CO2吸附反应的机理被认为包括K2CO3和MgO的快速水合,KHCO3的形成和分解,最后是Mg(OH)(2)的碳酸化,从而产生MgCO3作为主要产物。假设K2CO3通过K2CO3和KHCO3之间的可逆反应,为CO2和水提供了进入吸附剂核心区域的有效途径。 (C)2015 Elsevier Ltd.保留所有权利。

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