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首页> 外文期刊>International journal of hydrogen energy >Kinetics of the water-gas shift reaction over a La_(0.7)Ce_(0.2)FeO_3 perovskite-like catalyst using simulated coal-derived syngas at high temperature
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Kinetics of the water-gas shift reaction over a La_(0.7)Ce_(0.2)FeO_3 perovskite-like catalyst using simulated coal-derived syngas at high temperature

机译:模拟煤衍生合成气在La_(0.7)Ce_(0.2)FeO_3钙钛矿状催化剂上水煤气变换反应的动力学

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摘要

The kinetics of the water-gas shift (WGS) reaction over a novel La_(0.7)Ce_(0.2)FeO_3 perovskite-like catalyst is investigated using simulated coal-derived syngas at temperatures of 550 ℃ and 600 ℃ which are higher than the maximum operating temperature limit for conventional high temperature WGS catalysts. The influences of CO, CO_2, H_2O and H_2 concentration on WGS reaction rate are determined using selected gas compositions that might be encountered in a coal-based gasification system. An empirical power-law rate model used in this study is found to correlate well with experimental data with good accuracy. Kinetics parameters over La_(0.7)Ce_(0.2)FeO_3 obtained in this study are mostly in agreement with those previously measured using Fe-Cr based commercial catalysts in a range of relatively lower temperatures (300-500 ℃).
机译:使用模拟煤衍生的合成气,在最高温度550℃和600℃下,研究了新型La_(0.7)Ce_(0.2)FeO_3钙钛矿状催化剂上水煤气变换(WGS)反应的动力学。常规高温WGS催化剂的操作温度极限。使用煤基气化系统中可能遇到的选定气体成分,确定了CO,CO_2,H_2O和H_2浓度对WGS反应速率的影响。发现本研究中使用的经验幂律率模型与实验数据具有良好的相关性,并且具有良好的准确性。在这项研究中获得的La_(0.7)Ce_(0.2)FeO_3的动力学参数与先前使用Fe-Cr基商业催化剂在相对较低的温度范围(300-500℃)下测得的动力学参数基本一致。

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