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The influence of CO_2 gas concentration on the char temperature and conversion during oxy-fuel combustion in a fluidized bed

机译:流化床中氧燃料燃烧过程中CO_2气体浓度对焦炭温度和转化率的影响

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In spite of the extensive theoretical and experimental work carried out on coal/char oxy-combustion in a fluidized bed (FB), the effect of changing the atmosphere from O-2/N-2 to O-2/CO2 for a high O-2 concentrations is not entirely understood. In this work, experiments with single char particles are conducted in a bi-dimensional FB at 800 and 850 degrees C, varying the O-2 concentration from 11 to 50%(v/v) in N-2 or CO2. The FB reactor has a quartz window for visual observation, allowing the measurement of temperature and tracking the char conversion process by pyrometry with a digital camera. The method is shown to overcome the inherent limitations of other methods used in FB, such as thermocouples or pyrometry with an optical probe. Results indicate that the transfer of O-2 from the bulk gas of the bed to the surface of a char particle controls the overall rate of char conversion in O-2/N-2 and in O-2/CO2. In the latter gas mixture, the carbon consumption by gasification is significant even at a relatively low char temperature (850 degrees C). This additional carbon consumption makes the apparent char consumption rate in both atmospheres roughly equal (at the same O-2 concentration) for char temperatures below 925 degrees C, and higher in O-2/CO2 than in O-2/N-2 for char temperatures above 925 degrees C. Moreover, during the time in which the char stays in the emulsion phase, its temperature is roughly the same in both atmospheres, but when the char is in the bubble or splash zone its temperature is much higher than that in the emulsion phase. As a result, the difference in char conversion rate, observed in both atmospheres, is mainly controlled by the time in which the char particle is out of the emulsion phase. These results underline the importance of paying attention to the movement of a char particle through the different phases of the bed in order to improve the understanding of the oxy-fuel behavior in FB.
机译:尽管在流化床(FB)中对煤/焦炭的氧燃烧进行了大量的理论和实验工作,但对于高O,将气氛从O-2 / N-2变为O-2 / CO2的效果-2浓度尚不完全清楚。在这项工作中,在800和850摄氏度的二维FB中对单个炭颗粒进行了实验,将O-2在N-2或CO2中的浓度从11%更改为50%(v / v)。 FB反应器有一个用于目视观察的石英窗,可进行温度测量并通过数码相机的高温测定法跟踪焦炭转化过程。所显示的方法克服了FB中其他方法的固有局限性,例如热电偶或带有光学探针的高温测定法。结果表明,O-2从床中的大量气体转移到炭颗粒表面控制了O-2 / N-2和O-2 / CO2中炭转化的总速率。在后一种气体混合物中,即使在相对较低的焦炭温度(850摄氏度)下,通过气化的碳消耗量仍然很大。这种额外的碳消耗量使得在低于925摄氏度的焦炭温度下,两种气氛下的表观焦炭消耗率大致相等(在相同的O-2浓度下),而在O-2 / CO2中,其表观碳消耗率高于O-2 / N-2炭的温度高于925摄氏度。此外,在炭停留在乳液相的过程中,两种气氛的温度大致相同,但是当炭处于气泡或飞溅区时,其温度要比该温度高得多。在乳液相中。结果,在两种气氛中观察到的炭转化率的差异主要由炭颗粒脱离乳液相的时间控制。这些结果强调了关注炭颗粒在床层不同相中运动的重要性,以增进对FB中含氧燃料行为的了解。

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