曲雯雯, 夏洪应, 彭金辉, 张利波, 张正勇, 杨坤彬. 核桃壳热解特性及动力学分析[J]. 农业工程学报, 2009, 25(2): 194-198.
    引用本文: 曲雯雯, 夏洪应, 彭金辉, 张利波, 张正勇, 杨坤彬. 核桃壳热解特性及动力学分析[J]. 农业工程学报, 2009, 25(2): 194-198.
    Qu Wenwen, Xia Hongying, Peng Jinhui, Zhang Libo, Zhang Zhengyong, Yang Kunbin. Pyrolysis characteristics and kinetic analysis of walnut shell[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2009, 25(2): 194-198.
    Citation: Qu Wenwen, Xia Hongying, Peng Jinhui, Zhang Libo, Zhang Zhengyong, Yang Kunbin. Pyrolysis characteristics and kinetic analysis of walnut shell[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2009, 25(2): 194-198.

    核桃壳热解特性及动力学分析

    Pyrolysis characteristics and kinetic analysis of walnut shell

    • 摘要: 利用热重分析技术对核桃壳在高纯N2条件下的热解进行了分析,研究不同升温速率(5、10、20和40 K/min)对热解过程的影响,探讨了热解机理。研究表明,核桃壳非等温热解过程可分为失水干燥、快速热解和缓慢分解3个阶段,其中第二阶段是整个过程的主要部分,析出大量挥发分造成明显失重,随着升温速率的增加,最大热解速度提高,对应的峰值温度升高,差热热重分析(DTG)曲线肩峰中侧峰有所弱化,热滞后现象加重,热解各阶段向高温侧移动。快速热解阶段热解机理满足三维扩散Jander方程。不同升温速率下的活化能变化为102.28~117.73 kJ/mol,指前因子变化为4.13×106~2.42×108 min-1

       

      Abstract: The pyrolysis of walnut shell was carried out by means of the thermogravimetric method in high pure N2 atmosphere. The influences of different heating rates (5, 10, 20 and 40 K/min) on the pyrolysis process were investigated and the pyrolysis mechanism was discussed. The results show that the non-isothermal pyrolysis process of walnut shell includes three distinct stages: dehydration, fast-pyrolysis and residue slow decomposition. The second stage in which a huge amount of released volatile components caused the distinct weight loss of walnut shell played a main role in the whole process. With the increase of heating rate, the maximum decomposition rate and its corresponding temperatures of walnut shell increase. The TG curve and the peaks in DTG curve shift to higher temperatures due to the aggravating thermal lag. The pyrolysis processes are well described by the models of Jander equation and valid for diffusion control. The activation energies range from 102.28 to 117.73 kJ/mol and the pre-exponential factors vary from 4.13×106to2.42×108 min-1at different heating rates.

       

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