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TG-FTIR and kinetics of devolatilization of Sulcis coal

机译:TG-FTIR与Sulcis煤脱挥发分动力学

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The N_2-pyrolysis of low-rank Sulcis coal was investigated by thermogravimetric techniques (TG/DTG) in the temperature range ambient to 1000 ℃ under dynamic heating conditions (50, 75, and 100 ℃ min~(-1) heating rates). Little differences in the mass losses with heating rates were observed. From thermogravimetric analysis it was established that coal pyrolysis consisted of three main stages: water evaporation; devolatilization of thermally labile and more stable volatiles; and char formation. The evolved gas (EGA) by Fourier transform infrared spectrometry (FTIR) coupled to the thermobalance under 100 ℃min~(-1) heating rate was conducted for the identification of the gaseous species and their evolution profiles during coal thermal degradation. The temperatures of maximum rate of release of H_2O, CO_2, CO, COS, C_2 H_4, as well volatile fragments originating from breaking of covalent bonds such as alkyl and ether groups, were in agreement with the temperature of maximum mass-loss rate around 466 ℃. Meanwhile the maximum releasing rates of SO_2, CH_4, and NH_3 took place at 330, 575, and 690 ℃. respectively. An increase of CO emission intensity at 770 ℃ was indicating in situ gasification with CO_2 -bearing product of freshly formed char. The kinetic processing of non-isothermal TG data was performed by isoconversional method. In the coal conversion regions α = 5-40% the apparent activation energies were almost constant suggesting a single-step reaction path. The calculated average £ value was 189 kJ mol~(-1). A kinetic compensation effect existed between £ and In A: the linear dependence provided an average pre-exponential factor A_0 value of 2 × 10~(11) min~(-1). With further increase of conversion degree a complex £ dependence on α was evident as the coal thermal degradation process underwent a multi-step reactions.
机译:在动态加热条件下(50、75和100℃min〜(-1)加热速率),通过热重技术(TG / DTG)在低至1000℃的温度范围内研究了低阶Sulcis煤的N_2热解。观察到质量损失与加热速率几乎没有差异。从热重分析可以看出,煤的热解过程包括三个主要阶段:水的蒸发;水的蒸发;水的蒸发。热不稳定和更稳定的挥发物的脱挥发分;和炭形成。采用傅里叶变换红外光谱(FTIR)和100℃min〜(-1)加热速率下的热天平,对所产生的气体(EGA)进行了鉴定,以鉴定煤热降解过程中的气态种类及其演变特征。 H_2O,CO_2,CO,COS,C_2H_4的最大释放速率以及源自烷基和醚基等共价键断裂的挥发性片段的温度与最大质量损失速率的温度约466相符℃。同时,SO_2,CH_4和NH_3的最大释放速率分别为330、575和690℃。分别。 770℃CO排放强度的增加表明新鲜形成的焦炭的含CO_2的产物就地气化。非等温TG数据的动力学处理是通过等转换方法进行的。在煤转化率α= 5-40%时,表观活化能几乎恒定,表明存在一步反应路径。计算的平均£值为189 kJ mol〜(-1)。在£和In A之间存在动力学补偿效应:线性相关性提供的平均指数前因子A_0值为2×10〜(11)min〜(-1)。随着转化率的进一步提高,随着煤的热降解过程经历了多步反应,对α的复杂依赖性变得明显。

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