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The structure of a combustion front propagating in a fixed bed of crushed oil shale : co-current configuration

机译:在破碎油页岩固定床中传播的燃烧前沿结构:并流构型

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摘要

The structure of a combustion front propagating in a fixed bed of crushed oil shale: co-current configuration. The propagation of a combustion front in reactive porous medium involves thermal, chemical and fluid flow mechanisms, with strong couplings. In order to describe the thermal and chemical structure of the combustion front, a new experimental device, finely instrumented, allowing to carry out 1D experiments in co-current combustion was designed and developed. To validate the combustion cell, a porous medium model - a mix of charcoal/sand was used. This fixed bed down flow reactor is equipped with an original system that allows micro sampling gas within the combustion front. For the experiments with the oil shale from Timahdit in Morocco, it was crushed and sieved into particle size at 500-1000 µm and mixed with sand. The combustion was carried out at air velocity of 0.024 m s-1 at STP. The front propagates at 6.13x10-5 m s-1 and its temperature peak is 1100 °C. A mass balance was made based on a detailed chemical and physical characterization of the medium, its solid residue after combustion and flue gas. The organic matter is converted into 1/4 of fixed carbon – which the oxidation reactions provide the energy to propagate the front -1/4 into pyrolysis gas and 1/2 into oil. A two temperature numerical model developed by IMFT was validated. Combining, experimental and numerical approach made it possible in fine to evaluate the thickness of the different reaction zones: oil shale devolatilization, fixed carbon oxidation and CaCO3 decarbonation. A parametric study varying the air velocity and particle size is finally proposed
机译:在破碎的油页岩固定床中传播的燃烧前沿的结构:并流构型。燃烧前沿在反应性多孔介质中的传播涉及热,化学和流体流动机制,并具有强耦合性。为了描述燃烧前沿的热和化学结构,设计并开发了一种新的精密实验设备,可以进行并流燃烧的一维实验。为了验证燃烧室,使用了多孔介质模型-木炭/沙子的混合物。该固定床向下流动反应器配备有一个原始系统,该系统可以对燃烧前部的气体进行微量采样。为了进行摩洛哥提马迪迪(Timahdit)油页岩的实验,将其压碎并筛分成500-1000 µm的粒度,并与沙子混合。在STP下以0.024m s-1的空气速度进行燃烧。锋面以6.13x10-5 m s-1传播,其温度峰值为1100°C。根据对介质,燃烧后的固体残留物和烟道气的详细化学和物理特性进行质量平衡。有机物被转化为固定碳的1/4 –氧化反应提供了能量,使前-1/4扩散为热解气,而1/2扩散为油。验证了由IMFT开发的两个温度数值模型。结合实验和数值方法,可以很好地评估不同反应区的厚度:油页岩脱挥发分,固定碳氧化和CaCO3脱碳。最后提出了改变空气速度和粒径的参数研究

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    Ferreira Martins Marcio;

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  • 年度 2008
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