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Evolution of coal char porosity from CO_2-pyrolysis experiments

机译:CO_2热解实验中煤焦孔隙度的演变

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Pyrolysis experiments on a high volatile bituminous Columbian coal were performed in a laminar drop tube reactor at T = 1300 K and 1475 K. Measurements in CO2 were carried out at different residence times up to 150 ms, and the data were complemented by end-point measurements in N-2 at approximately 165 ms. These low residence times are typical for the duration of pyrolysis in pulverized coal flames. Mass loss has been determined by solid sampling based on the ash tracer method, and the evolution of porosity was evaluated. Pyrolysis mass loss kinetics were determined based on a single first order reaction and a competing two-step reaction model with distributed activation energies. The particle temperature and residence time needed for the determination of the kinetics were derived by CFD simulations. Results indicate that, despite the low residence time selected, the influence of the Boudouard reaction on mass loss and, hence, evolution of porosity cannot be neglected. In general, porosity increases with increasing residence time and progressing mass loss and porosity is influenced by the both, the release of volatiles and the contribution of gasification.
机译:在层流式滴管反应器中于T = 1300 K和1475 K上对高挥发性烟煤哥伦比亚煤进行了热解实验。在不超过150 ms的不同停留时间下进行了CO2测量,并通过端点对数据进行了补充在N-2中大约165毫秒进行测量。这些低的停留时间对于煤粉火焰中的热解持续时间是典型的。通过基于灰示踪法的固体采样确定了质量损失,并评估了孔隙度的演变。基于单个一级反应和具有分布活化能的竞争性两步反应模型确定热解质量损失动力学。确定动力学所需的颗粒温度和停留时间是通过CFD模拟得出的。结果表明,尽管选择了低停留时间,但不能忽略Boudouard反应对质量损失的影响,因此不能忽略孔隙的演变。通常,孔隙率随停留时间的增加和质量损失的增加而增加,孔隙率受挥发物的释放和气化作用的影响。

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