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Kinetic study of polish hard coal and its char gasification using carbon dioxide

机译:抛光硬煤的动力学研究及其使用二氧化碳进行焦化气化

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摘要

The kinetics of polish hard coal and its char gasification using carbon dioxide as gasifying agent was studied at atmospheric pressure between 293 and 1223 K at different linear heating rates. Calculations using isoconversional method showed that coal gasification has two separate steps: pyrolysis in the range from 600 to 850 K and gasification in the range from 1000 to 1273 K. This proves the additivity of pyrolysis and gasification steps. The apparent activation energy calculated using the F1 model for coal char gasification is equal to 245 kJ/mol, and log A is equal to 7.4 1/s, which is similar to the value obtained by the isoconversional method. Coal gasification reaction with carbon dioxide is faster and takes place in a lower temperature range than the gasification process of the char obtained in a separate process. The stabilized and chemically deactivated char is harder to gasify, and the same conversion is achieved at the higher temperature. The estimated shift may be as high as 150 K.
机译:研究了硬质煤的抛光动力学及其使用二氧化碳作为气化剂进行焦化气化的过程,该研究在大气压力为293至1223 K的线性加热速率下进行。使用等转化方法的计算表明,煤气化有两个独立的步骤:600至850 K范围内的热解和1000至1273 K范围内的气化。这证明了热解和气化步骤的可加性。使用F1模型计算出的煤焦气化的表观活化能等于245 kJ / mol,log A等于7.4 1 / s,这与通过等转化法获得的值相似。与在单独的过程中获得的焦炭的气化过程相比,用二氧化碳进行的煤气化反应更快并且在较低的温度范围内进行。稳定且化学失活的炭更难气化,并且在较高温度下可实现相同的转化率。估计的偏移可能高达150K。

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