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Characterization study and five-cycle tests in a fixed-bed reactor of titania-supported nickel oxide as oxygen carriers for the chemical-looping combustion of methane

机译:二氧化钛负载的氧化镍作为氧气载体进行甲烷化学循环燃烧的固定床反应器的表征研究和五周期试验

摘要

Recent investigations have shown that in the combustion of carbonaceous compounds CO2 and NOx emissions to the atmosphere can be substantially reduced by using a two-stage chemical-looping process. In this process, the reduction stage is undertaken in a first reactor in which the framework oxygen of a reducible inorganic oxide is used, instead of the usual atmospheric oxygen, for the combustion of a carbonaceous compound, for instance, methane. The outlet gas from this reactor is mostly composed of CO2 and steam as reaction products and further separation of these two components can be carried out easily by simple condensation of steam. Then, the oxygen carrier found in a reduced state is transported to a second reactor in which carrier regeneration with air takes place at relatively low temperatures, consequently preventing the formation of thermal NOx. Afterward, the regenerated carrier is carried to the first reactor to reinitiate a new cycle and so on for a number of repetitive cycles, while the carrier is able to withstand the severe chemical and thermal stresses involved in every cycle. In this paper, the performance of titania-supported nickel oxides has been investigated in a fixed-bed reactor as oxygen carriers for chemical-looping combustion of methane. Samples with different nickel oxide contents were prepared by successive incipient wet impregnations, and their performance as oxygen carriers was investigated at 900 °C and atmospheric pressure in five-cycle fixed-bed reactor tests using pure methane and pure air for the respective reduction and regeneration stages. The evolution of the outlet gas composition in each stage was followed by gas chromatography, and the involved chemical, structural, and textural changes of the carrier in the reactor bed were studied by using different characterization techniques. From the study, it is deduced that the reactivity of these nickel-based oxygen carriers is in the two involved stages and almost independent of the nickel loading. However, in the reduction stage, carbon deposition, from the thermal decomposition of methane, and CO emissions, mainly derived from the partial reduction of titania as support acting as an additional oxygen source, may impose some constraints to the efficiency of the overall chemical-looping combustion process in CO 2 capture. © 2005 American Chemical Society.
机译:最近的研究表明,在碳质化合物的燃烧中,通过使用两步化学循环工艺,可以大大减少向大气排放的CO2和NOx。在该方法中,还原步骤在第一反应器中进行,在该反应器中,使用可还原的无机氧化物的骨架氧代替通常的大气氧来燃烧含碳化合物,例如甲烷。来自该反应器的出口气体主要由作为反应产物的CO 2和蒸汽组成,并且通过简单的蒸汽冷凝可以容易地进一步分离这两种组分。然后,将处于还原状态的氧气载体输送到第二反应器,在该反应器中,在相对较低的温度下用空气进行载体再生,从而防止了热氮氧化物的形成。之后,将再生的载体带入第一反应器以重新开始新的循环,如此重复多个循环,而该载体能够承受每个循环中所涉及的严重的化学和热应力。在本文中,已经在固定床反应器中研究了二氧化钛负载的氧化镍作为甲烷化学循环燃烧的氧气载体的性能。通过连续初期湿法浸渍制备具有不同氧化镍含量的样品,并在五循环固定床反应器测试中使用纯甲烷和纯空气分别还原和再生,在900°C和大气压下研究了它们作为氧气载体的性能。阶段。气相色谱法跟踪每个阶段出口气体组成的变化,并通过使用不同的表征技术研究了反应器床中载体所涉及的化学,结构和结构变化。从研究中可以推断出,这些镍基氧载体的反应性处于两个相关阶段,并且几乎与镍的载量无关。但是,在还原阶段,甲烷的热分解产生的碳沉积和CO的排放(主要来自作为载体的二氧化钛作为额外氧气源的部分还原)可能会对整体化学反应的效率产生一些限制。 CO 2捕集中的循环燃烧过程。 ©2005美国化学学会。

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