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A semi-empirical approach towards predicting producer gas composition in biomass gasification

机译:预测生物质气化生产者气体组合物的半实验方法

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摘要

The paper provides a comparison of five distinct models, often used in thermodynamic equilibrium modeling that allows the study of feedstock effect on gasification process. The five models were thus formulated and solved using MATLAB software. The results were compared with published experimental data. The model based on equilibrium constant derived using methane formation reaction and water gas shift reaction showed comparatively better performance. Once the model was selected, the response surface analysis was employed to predict the parameters, such as reactor temperature and feedstock moisture content, for a maximum heating value of the producer gas. Simulations were performed for 50 different biomass feedstocks and simplified correlations were developed from simulated producer gas composition using multiple linear regression. These correlations may be suited for the quick comparison of different feedstocks in gasification process.
机译:本文提供了五种不同模型的比较,通常用于热力学平衡建模,允许研究原料过程对气化过程的影响。 因此,使用MATLAB软件配制并解决了五种模型。 将结果与公开的实验数据进行比较。 基于使用甲烷形成反应衍生的平衡常数的模型和水煤气变换反应显示相对较好的性能。 一旦选择模型,就采用响应表面分析来预测生产者气体的最大加热值,例如反应器温度和原料水分含量的参数。 对50种不同的生物质原料进行模拟,并从使用多元线性回归从模拟生产者气体组合物中产生简化的相关性。 这些相关性可以适用于在气化过程中的不同原料的快速比较。

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