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首页> 外文期刊>Journal of Analytical & Applied Pyrolysis >Effect of atmosphere reaction and heating rate on the devolatilization of a Colombian sub-bituminous coal
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Effect of atmosphere reaction and heating rate on the devolatilization of a Colombian sub-bituminous coal

机译:大气反应和升温速率对哥伦比亚次烟煤脱挥发分的影响

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摘要

This work studies the combined effect of heating rate and reaction atmosphere on the devolatilization of sub-bituminous type A coal (SubbA coal). Non-isothermal thermogravimetric analysis (TGA) was performed on SubbA coal undergoing pyrolysis. Mass loss dataset was fit to a lumped kinetic model using two different model-free fitting methods (FWO and Vyazovkin). Meaningful differences were obtained in devolatilization kinetics under N-2 (traditional combustion) and CO2 (oxy-combustion process with gas recirculation). Through TGA it was found that at low heating rates, the pyrolysis mass loss rate is higher in N-2 than in CO2. Based on the activation energy distribution, CHN analysis on residual char, and tracking the evolution of products in gaseous phase during devolatilization in CO2, it was demonstrated that at temperatures higher than 660 degrees C, CO2 reacts with the formed char. This gasification reaction becomes a controlling stage of the thermochemical transformation in CO2. Additional pyrolysis experiments were conducted in a fast-heating hot plate reactor (HPR) with 2 mm particles in N-2 and CO2 using heating rates between 50 degrees C/s and 1200 degrees C/s. These higher heating rates are similar to those of fluidized beds. In the HPR experiments, devolatilization is more intense for CO2 than N-2. Differences arising from the two environments are likely caused by the different thermal and diffusive properties of both gases. (C) 2016 Elsevier B.V. All rights reserved.
机译:这项工作研究了加热速率和反应气氛对亚沥青A型煤(SubbA煤)的脱挥发分的综合影响。对进行热解的SubbA煤进行了非等温热重分析(TGA)。使用两种不同的无模型拟合方法(FWO和Vyazovkin)将质量损失数据集拟合到集总动力学模型。在N-2(传统燃烧)和CO2(带有气体再循环的氧气燃烧过程)下,脱挥发分动力学获得了显着差异。通过TGA,发现在低加热速率下,N-2的热解质量损失率高于CO2。基于活化能分布,CHN分析残余炭并跟踪CO2脱挥发分过程中气相产物的演变,证明了在高于660摄氏度的温度下,CO2与生成的炭发生反应。该气化反应成为CO 2中热化学转化的控制阶段。在50°C / s至1200°C / s的加热速率下,在N-2和CO2中具有2 mm颗粒的快速加热热板反应器(HPR)中进行了其他热解实验。这些较高的加热速率类似于流化床的加热速率。在HPR实验中,CO2的脱挥发分比N-2更强烈。两种环境产生的差异很可能是由于两种气体的热和扩散特性不同所致。 (C)2016 Elsevier B.V.保留所有权利。

著录项

  • 来源
    《Journal of Analytical & Applied Pyrolysis》 |2016年第9期|93-101|共9页
  • 作者单位

    Univ Nacl Colombia, Fac Minas, Grp Termodinam Aplicada & Energias Alternat, Escuela Quim & Petr, Carrera 80 65-223, Medellin, Colombia;

    Univ Nacl Colombia, Fac Minas, Grp Termodinam Aplicada & Energias Alternat, Escuela Quim & Petr, Carrera 80 65-223, Medellin, Colombia;

    Univ Nacl Colombia, Fac Minas, Grp Termodinam Aplicada & Energias Alternat, Escuela Quim & Petr, Carrera 80 65-223, Medellin, Colombia;

    Univ Nacl Colombia, Fac Minas, Grp Termodinam Aplicada & Energias Alternat, Escuela Quim & Petr, Carrera 80 65-223, Medellin, Colombia;

    Univ Nacl Colombia, Fac Minas, Grp Termodinam Aplicada & Energias Alternat, Escuela Quim & Petr, Carrera 80 65-223, Medellin, Colombia;

  • 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-combustion; Combustion; Devolatilization; Model-free methods; Kinetics of devolatilization;

    机译:氧燃烧;燃烧;脱挥发分;无模型方法;脱挥发分动力学;

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