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Improving the efficiency of Chemical Looping Combustion with coal by using ring-type internals in the fuel reactor

机译:通过在燃料反应堆中使用环形内部构件来提高煤化学循环燃烧的效率

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Chemical Looping Combustion (CLC) with solid fuels has been widely developed by using two interconnected fluidized beds, the fuel reactor and the air reactor, with an oxygen carrier continuously circulating between them. Experience gained in this process shows that high CO2 capture values can be reached. However, complete combustion of the fuel is not achieved, with some H-2, CO and CH4 as the main unconverted compounds in the combustion products from the fuel reactor. It is believed that the combustion efficiency can be increased by improving the gas-solid contact in the fuel reactor. In this work, the solids distribution in the fuel reactor was modified by using ring-type internals with the objective of enhancing the gas-solid contact. Two experimental campaigns were carried out in a 50 kWth CLC unit burning a bituminous coal with ilmenite particles in the temperature interval of 900-1000 degrees C. The first campaign was conducted with the original riser of the fuel reactor, which was characterized by a smooth section from bottom to top. For the second campaign, three ring-type internals were implemented in the riser in order to modify the solids distribution in the fuel reactor. The presence of the internals had a beneficial effect on the coal combustion. The major benefit was an improved oxidation of volatile matter in the form of CH4 and the full conversion of H-2. As a result, the total oxygen demand decreased by 20%, from 12.2% to 9.8%, with the implementation of the internals.
机译:通过使用两个相互连接的流化床,燃料反应器和空气反应器,并在它们之间不断循环的氧气载体,已广泛开发了具有固体燃料的化学回路燃烧(CLC)。在此过程中获得的经验表明,可以实现较高的CO2捕集值。但是,由于燃料反应堆燃烧产物中的一些H-2,CO和CH4是主要的未转化化合物,因此无法实现燃料的完全燃烧。认为可以通过改善燃料反应器中的气固接触来提高燃烧效率。在这项工作中,以增强气固接触为目的,通过使用环形内部构件来改变燃料反应堆中的固体分布。在50千瓦时CLC装置中进行了两次实验,在900-1000摄氏度的温度区间内燃烧了含钛铁矿颗粒的烟煤。第一个实验是使用燃料反应器的原始立管进行的,其特点是平稳从下到上。对于第二个活动,在立管中采用了三个环形内部构件,以改变燃料反应堆中的固体分布。内部构件的存在对煤燃烧具有有益的影响。主要好处是改进了CH4形式的挥发性物质的氧化和H-2的完全转化。结果,采用内部结构后,总氧气需求量从12.2%下降到9.8%,降低了20%。

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