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首页> 外文期刊>Energy Conversion & Management >Equilibrium modeling of gasification: Gibbs free energy minimization approach and its application to spouted bed and spout-fluid bed gasifiers
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Equilibrium modeling of gasification: Gibbs free energy minimization approach and its application to spouted bed and spout-fluid bed gasifiers

机译:气化平衡模型:吉布斯自由能最小化方法及其在喷床和喷流床气化炉中的应用

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摘要

Spouted beds have been found in many applications, one of which is gasification. In this paper, the gasification processes of conventional and modified spouted bed gasifiers were considered. The conventional spouted bed is a central jet spouted bed, while the modified spouted beds are circular split spouted bed and spout-fluid bed. The Gibbs free energy minimization method was used to predict the composition of the producer gas. The major six components, CO, CO_2, CH_4, H_2O, H_2 and N_2, were determined in the mixture of the producer gas. The results showed that the carbon conversion in the gasification process plays an important role in the model. A modified model was developed by considering the carbon conversion in the constraint equations and in the energy balance calculation. The results from the modified model showed improvements. The higher heating values (HHV) were also calculated and compared with the ones from experiments. The agreements of the calculated and experimental values of HHV, especially in the case of the circular split spouted bed and the spout-fluid bed were observed.
机译:在许多应用中已经发现喷射床,其中之一是气化。在本文中,考虑了常规和改进的喷射床气化炉的气化过程。传统的喷射床是中央喷射喷射床,而改进的喷射床是圆形分流喷射床和喷射流体床。吉布斯自由能最小化方法用于预测生产气的组成。在生产气的混合物中确定了主要的六种成分,CO,CO_2,CH_4,H_2O,H_2和N_2。结果表明,气化过程中的碳转化率在模型中起重要作用。通过在约束方程式和能量平衡计算中考虑碳转化率,开发出一种改进的模型。修改后的模型的结果显示出改进。还计算出较高的发热量(HHV),并将其与实验结果进行比较。观察到HHV的计算值和实验值的一致性,尤其是在圆形分流喷头床和喷流床中。

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