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    氢溢流强化菱镁矿热解耦合逆水煤气反应研究

    Promoting dolomite pyrolysis coupled with reverse water-gas shift reaction through hydrogen spillover

    • 摘要: 为降低耐材工业生产中菱镁矿(主要成分MgCO3)热分解过程的能耗与碳排放,研究了菱镁矿热解耦合催化加氢的节能减碳效果,并探讨了氢溢流对该过程的强化机制。结果表明催化剂的添加对菱镁矿分解率和CO2转化率有显著影响,尤其是对于RuNi/TiO2/CeO2催化剂,其在合成过程中原位形成的TiO2可以通过调控SMSI效应促进活性组分Ni还原,增强催化剂的氢溢流效应,从而高效的将CO2转化为CO,促进菱镁矿分解反应平衡正向移动。实现在500 ℃条件下,菱镁矿分解率达到83.17%,CO2转化率达到55.58%,CO选择性>99%,较参比催化剂RuNi/CeO2 (71.09%、42.36%、84.12%)有显著提升。磁选分离实验表明RuNi/TiO2/CeO2催化剂可以与固态产物有效分离,回收率大于95%。原位DRIFTS表征发现*COOH物种是该过程的关键中间体,其进一步解离为CO。

       

      Abstract: Abstract: To reduce energy consumption and carbon emissions during the thermal decomposition of magnesite (primarily composed of MgCO3) in the production of refractory materials, the energy-saving and carbon-reducing effects of coupling magnesite pyrolysis with catalytic hydrogenation were investigated. Additionally, the role of hydrogen spillover in enhancing this process was explored. The results demonstrated that the addition of a catalyst had a significant impact on both magnesite decomposition and CO2 conversion, particularly with the RuNi/TiO2/CeO2 catalyst. The TiO2 that form in situ during the synthesis process can enhance hydrogen spillover, which efficiently converts CO2 into CO and helps shift the magnesite decomposition equilibrium to the forward direction. Under conditions of 500 ℃, the decomposition of magnesite reached 83.17%, CO2 conversion reached 55.58%, and CO selectivity exceeded 99%, showing a notable improvement over the reference catalyst RuNi/CeO2 (71.09%, 42.36%, 84.12%). Magnetic separation experiments confirmed that the RuNi/TiO2/CeO2 catalyst could be effectively separated from the solid products, with a recovery rate of over 95%. In situ DRIFTS characterization revealed that *COOH species are key intermediates, which further dissociate into CO.

       

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