Non-catalytic heterogeneous combustion and gasification reactions modeling for a single char pellet

IF 3.7 3区 工程技术 Q2 ENGINEERING, CHEMICAL
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引用次数: 0

Abstract

The objective of the present study was to analyze the gasification process for the simultaneous exposure to a multi-component gasifying mixture. In a real scenario of the gasification process, char pellets from the pyrolysis zone undergo multiple non-catalytic gas-solid reactions in combustion and gasification zones. A single-char pellet gasification and combustion is studied in this study. This was done by developing a mathematical formulation, based on a grain model, for multiple reactions that also incorporated transient and non-isothermal behaviors, structural changes, and porosity changes. The developed model was validated against experimental data from the literature and was in good agreement. The variation of conversion, gasification reactivity, species’ effectiveness factor, and reactions’ effectiveness factor for various parameters were analyzed. Out of these parameters, bulk temperature, initial condition for temperature, pellet radius, and diffusivity of the gases were found to have a profound impact on the effectiveness factor of the species.

单个炭粒的非催化异相燃烧和气化反应建模
本研究的目的是分析同时接触多组分气化混合物的气化过程。在实际的气化过程中,来自热解区的木炭颗粒会在燃烧区和气化区发生多种非催化气固反应。本研究对单炭颗粒气化和燃烧进行了研究。在此基础上,开发了基于晶粒模型的多种反应数学公式,其中还包括瞬态和非等温行为、结构变化和孔隙率变化。所建立的模型与文献中的实验数据进行了验证,结果吻合良好。分析了各种参数对转化率、气化反应性、物种有效因子和反应有效因子的影响。在这些参数中,体积温度、温度的初始条件、颗粒半径和气体的扩散性对物种的有效因子有很大影响。
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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