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Pyrolysis characteristics and kinetics of sewage sludge for different sizes and heating rates

机译:不同粒径和升温速率下污泥的热解特性和动力学

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The pyrolysis characteristics and kinetics of sewage sludge for different sizes (d < 0.25 mm, 0.25 mm < d < 0.83 mm, and d > 0.83 mm) and heating rates (5, 20, and 35 °C/min) were investigated in this article. The STA 409 was utilized for the sewage sludge thermogravimetric analysis. FTIR analysis was employed to study the functional groups and intermediates during the process of pyrolysis. Meanwhile, a new method was developed to calculate pyrolysis kinetic parameters (activated energy E, the frequency factor A, and reaction order n) with surface fitting tool in software MATLAB. The results show that all the TG curves are divided into three stages: evaporation temperature range (180-220 °C), main decomposition temperature range (220-650 °C), and final decomposition temperature range (650-780 °C). The sewage sludge of d < 0.25 mm obtains the largest total mass loss, especially at the heating rate of 5 °C/min. By FTIR analysis, the functional groups including NH, C-H, C=C, etc., are all found in the sewage sludge. There is a comparison between the FTIR spectra of sludge heated to 350 °C (temperature associated to maximum devolatilization rate in the second stage) and the FTIR spectra of sludge heated to 730 °C (temperature associated to maximum devolatilization rate in the third stage). In the second stage, the alcohols, ammonia, and carboxylic acid in the sludge have been mostly decomposed into gases, and only a little bit of compounds containing CH and OH of COOH exist. The pyrolysis kinetic parameters of second stage are as follows: the reaction orders are in the range of 1.6-1.8 and the activation energy is about 45 kJ/mol. The frequency factor increases with the increase of heating rate and sewage sludge size.
机译:在此研究了不同尺寸(d <0.25 mm,0.25 mm 0.83 mm)和加热速率(5、20和35°C / min)的污泥的热解特性和动力学。文章。 STA 409用于污水污泥的热重分析。 FTIR分析用于研究热解过程中的官能团和中间体。同时,开发了一种利用MATLAB软件中的表面拟合工具计算热解动力学参数(活化能E,频率因子A和反应阶数n)的新方法。结果表明,所有TG曲线均分为三个阶段:蒸发温度范围(180-220℃),主要分解温度范围(220-650℃)和最终分解温度范围(650-780℃)。 d <0.25 mm的污水污泥获得最大的总质量损失,尤其是在5°C / min的加热速率下。通过FTIR分析,在污水污泥中发现了包括NH,C-H,C = C等的官能团。加热到350°C的污泥的FTIR光谱(第二阶段与最大挥发度相关的温度)与加热到730°C的污泥的FTIR光谱(第三阶段与最大挥发度相关的温度)之间进行比较。在第二阶段中,污泥中的醇,氨和羧酸大部分已分解为气体,并且仅存在少量的含有CHOH和COOH的化合物。第二阶段的热解动力学参数如下:反应级数在1.6-1.8范围内,活化能约为45kJ / mol。频率因数随着加热速率和污水污泥尺寸的增加而增加。

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