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A new technique for the measurement of theproduct CO/CO2 ratio at the surface of charparticles burning in a fluidized bed

机译:测量流化床中燃烧的炭颗粒表面产物CO / CO2比的新技术

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A new experimental technique is proposed to measure the product CO/CO2 ratio at the surface of sphericalchar particles during fluidized bed combustion. It is based on the measurement of the burning rate of asingle char particle under low oxygen concentration conditions and on the use of an accurate prediction ofthe particle Sherwood number. This technique was applied to spherical char particles obtained from a bituminouscoal which is characterized by a low attrition and fragmentation propensity. The product CO/CO2ratio was measured at a bed temperature of 850 °C and at a fluidization velocity of 0.3 m/s in a lab-scaleapparatus operated with a bed of 0.5–0.6 mm sand. The char particle size was varied between 2 and 7 mmand the inlet oxygen concentration between 0.1% and 2.0%. Results showed that under the experimentalconditions investigated carbon was mostly oxidized to CO2 within the particle boundary layer, with amaximum fraction of carbon escaping as CO of 10–20% at the lowest oxygen concentrations and largestparticle sizes.
机译:提出了一种新的实验技术来测量球形表面的产品CO / CO2比 流化床燃烧过程中炭颗粒。它基于对燃烧速率的测量 在低氧浓度条件下使用单个炭颗粒并精确预测 粒子舍伍德数。将该技术应用于从沥青中获得的球形炭颗粒 煤的特点是磨损和破碎倾向低。产品CO / CO2 在实验室规模下,在850°C的床温和0.3 m / s的流化速度下测量该比值 仪器在0.5-0.6 mm的砂层上运行。炭的粒径在2到7毫米之间变化 入口氧气浓度在0.1%至2.0%之间。结果表明,根据实验 在所研究的条件下,碳大部分在颗粒边界层内被氧化成CO2, 在最低的氧气浓度和最大的氧气浓度下,最大的碳逸出率为10–20% 粒度。

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