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Combustion of Pulverized Size Fuel Particles under Oxygen-Enriched Conditions with Overlap of Devolatilization and Char Oxidation

机译:富含氧化条件下粉碎尺寸燃料颗粒的燃烧,具有脱挥发化和炭氧化重叠

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The combustion characteristics of pulverized biomass particles, produced at a gas temperature of 1350 K and at discrete oxygen concentrations in the range of ppm levels - 48 percent, by volume, were investigated in an entrained laminar flow reactor. The particles experienced high heating rates during devolatilization, on the order 1 centre dot 105 K/s, and during char oxidation, particle burned at rates limited by the combined effects of pore diffusion and chemical reaction, i.e., under zone II burning conditions. In order to quantify reactivities and possible carbon deactivation during the combustion of biomass chars under zone II conditions, chars extracted at successive residence times from the flow reactor were subjected to oxygen reactivity tests in a pressurized thermogravimetric analyzer (PTGA). Oxygen levels in the TGA were maintained at a constant value of 6 percent, by volume, and temperatures were limited to about 723 K to ensure that reactivities were measured under kinetically-controlled (zone I) conditions. Measured conversion rates during oxidation tests under zone I burning conditions were combined with surface area measurements to yield intrinsic reactivities as a function of char conversion. The intrinsic char reactivities were characterized using a four-step heterogeneous reaction mechanism, a modification of a previously published reaction mechanism for carbon oxidation based on a density functional study of the chemisorption of oxygen on graphite surfaces. The Arrhenius parameters determined for the reactions in the mechanism yielded predicted mass loss rates at 1350 K that explained the mass loss rates in the laminar flow reactor tests.
机译:在1350k的气体温度下产生的粉碎生物质颗粒的燃烧特性,并在PPM水平的离散氧浓度下,在夹带的层流反应器中研究了PPM水平-48%的氧气浓度。颗粒在脱挥发型期间经历了高加热速率,在促进中心点105k / s,并且在Char氧化期间,以孔扩散和化学反应的速率限制为限制的颗粒,即在区域II燃烧条件下。为了在区域II条件下的生物质燃烧过程中量化反应性和可能的​​碳去激活,在加压热重分析仪(PTGA)中,在从流体反应器中逐次提取的氧反应性试验。 TGA中的氧水平以恒定值为6%,体积计,温度限于约723k,以确保在动力学(区域I)条件下测量反应性。在区域I燃烧条件下氧化试验期间测定的转化率与表面积测量结合,以产生固有的反应性作为Char转换的函数。使用四步非均相反应机制表征了本型焦炭反应性,这是基于石墨表面上氧的化学吸附的密度泛函研究的先前公布的碳氧化反应机理的改性。确定机构反应的Arrhenius参数在1350K中产生预测的质量损失率,该损失在层流体反应器试验中解释了大质量损失率。

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