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Modeling of coal gasification in an internally circulating fluidized bed reactor with draught tube

机译:带引流管的内部循环流化床反应器中煤气化的建模

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摘要

A predictive mathematical model is proposed based on the bed hydrodynamics, reaction kinetics and the empirical correlation of pyrolysis yields to predict gasification characteristics in an internally circulating fluidized bed gasifier with a draught tube. With the justifiable assumptions, steady state mathematical equations are derived and solved numerically. The simulated results of product gas composition, gas yield, carbon conversion, cold gas efficiency and calorific value of the product gas in each reaction region are compared with the obtained experimental data. The proposed model can explain the reaction behavior in the present reactor system within the range of variables studied.
机译:根据床的流体动力学,反应动力学和热解率的经验相关性,提出了一种预测数学模型,以预测带有引流管的内部循环流化床气化炉的气化特性。在合理的假设下,稳态数学方程式被导出并通过数值求解。将每个反应区域中产物气的组成,气体产率,碳转化率,冷气效率和产物气的热值的模拟结果与获得的实验数据进行了比较。所提出的模型可以在所研究的变量范围内解释本反应器系统中的反应行为。

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