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Devolatilization of a single fuel particle in a fluidized bed under oxy-combustion conditions. Part B: Modeling and comparison with measurements

机译:单一燃料颗粒在氧燃烧条件下在流化床中的脱挥发分。 B部分:建模和测量比较

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摘要

A detailed one-dimensional transient model is developed to describe the conversion of a single fuel particle in O-2/N-2 and O-2/CO2 atmospheres in a fluidized bed (FB). The model takes into account the main relevant phenomena occurring from the addition of a particle to the FB up to the instant when most of the volatiles have been released. The model accounts for the rates of drying, fuel devolatilization, homogeneous combustion of volatiles in a thin flame, heterogeneous combustion of char, and mass and heat transfer, the latter involving the heat transfer from the FB reactor and flame to the particle. The model is used to simulate and explain the experiments given in Part A of the present work, which includes tests with four ranks of coal (from anthracite to lignite) and one type of wood in O-2/N-2 and O-2/CO2 atmospheres with the O-2 volume concentration varying in the range of 0-40% at a fixed bed temperature of 1088 K. The predicted history of the temperature of the fuel particle and of the volatiles flame agrees well with the measurements. The simulated results indicate that the heat transfer processes at the particle scale are similar in pure N-2 and CO2. The model reveals that only a small amount of heat from the flame is transferred to the fuel particle, explaining why the rate of particle heating is hardly affected by the flame. The decrease in the devolatilization time measured at higher O-2 concentration is explained by heterogeneous (char) combustion, which is seen to be significant during the last stages of devolatilization. The model shows that the char combustion is limited by the rate of diffusion of O-2 to the particle and justifies the lower heating rate observed in O-2/CO2 compared to in O-2/N-2. A sensitivity analysis shows that the thermal capacity and conductivity of the fuel, as well as the convective heat transfer coefficient, are the most influencing parameters affecting the time of devolatilization. (C) 2014 The Combustion Institute. Published by Elsevier Inc. All rights reserved.
机译:建立了详细的一维瞬态模型来描述流化床(FB)中O-2 / N-2和O-2 / CO2气氛中单个燃料颗粒的转化。该模型考虑了从向FB添加颗粒到释放出大部分挥发物的瞬间发生的主要相关现象。该模型考虑了干燥速率,燃料挥发,稀薄火焰中挥发物的均匀燃烧,炭的不均匀燃烧以及质量和热传递,后者涉及从FB反应器和火焰到颗粒的热传递。该模型用于模拟和解释本工作A部分中给出的实验,其中包括使用4种煤(从无烟煤到褐煤)和一种类型的O-2 / N-2和O-2木材进行的测试。 / CO2气氛中O-2的体积浓度在1088 K的固定床温度下在0-40%的范围内变化。燃料颗粒和挥发物火焰的温度预测历史与测量值非常吻合。模拟结果表明,在纯N-2和CO2中,颗粒级的传热过程相似。该模型表明,火焰中只有少量热量传递给燃料颗粒,这说明了为什么火焰几乎不影响颗粒加热的速率。在更高的O-2浓度下测得的脱挥发分时间的减少可以通过异质(炭)燃烧来解释,这在脱挥发分的最后阶段很明显。该模型表明,炭燃烧受到O-2扩散到颗粒的速率的限制,并且证明了与在O-2 / N-2中相比,在O-2 / CO2中观察到的较低的加热速率是合理的。敏感性分析表明,燃料的热容量和电导率以及对流传热系数是影响脱挥发分时间的最大影响参数。 (C)2014年燃烧研究所。由Elsevier Inc.出版。保留所有权利。

著录项

  • 来源
    《Combustion and Flame》 |2015年第3期|809-818|共10页
  • 作者单位

    Southeast Univ, Key Lab Energy Thermal Convers & Control, Minist Educ, Sch Energy & Environm, Nanjing 210096, Jiangsu, Peoples R China|Chalmers, Environm & Energy Dept, S-41296 Gothenburg, Sweden;

    Chalmers, Environm & Energy Dept, S-41296 Gothenburg, Sweden;

    Southeast Univ, Key Lab Energy Thermal Convers & Control, Minist Educ, Sch Energy & Environm, Nanjing 210096, Jiangsu, Peoples R China;

    Univ Seville, Chem & Environm Engn Dept, Seville 41092, Spain;

    Southeast Univ, Key Lab Energy Thermal Convers & Control, Minist Educ, Sch Energy & Environm, Nanjing 210096, Jiangsu, Peoples R China;

    Chalmers, Environm & Energy Dept, S-41296 Gothenburg, Sweden;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Oxy-fuel; Devolatilization; Modeling; Fluidized bed; Coal; Biomass;

    机译:含氧燃料;挥发;建模;流化床;煤;生物质;
  • 入库时间 2022-08-18 00:11:08

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