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Modelling of combustion and sorbent reactions in three-dimensional flow environment of a circulating fluidized bed furnace

机译:循环流化床炉三维流动环境中燃烧和吸附剂反应的建模

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摘要

This thesis presents a three-dimensional, semi-empirical, steady state model for simulating the combustion, gasification, and formation of emissions in circulating fluidized bed (CFB) processes. In a large-scale CFB furnace, the local feeding of fuel, air, and other input materials, as well as the limited mixing rate of different reactants produce inhomogeneous process conditions. To simulate the real conditions, the furnace should be modelled three-dimensionally or the three-dimensional effects should be taken into account. The only available methods for simulating the large CFB furnaces three-dimensionally are semi-empirical models, which apply a relatively coarse calculation mesh and a combination of fundamental conservation equations, theoretical models and empirical correlations. The number of such models is extremely small. The main objective of this work was to achieve a model which can be applied to calculating industrial scale CFB boilers and which can simulate all the essential sub-phenomena: fluid dynamics, reactions, the attrition of particles, and heat transfer. The core of the work was to develop the model frame and the required sub-models for determining the combustion and sorbent reactions. The objective was reached, and the developed model was successfully used for studying various industrial scale CFB boilers combusting different types of fuel. The model for sorbent reactions, which includes the main reactions for calcitic limestones, was applied for studying the new possible phenomena occurring in the oxygen-fired combustion. The presented combustion and sorbent models and principles can be utilized in other model approaches as well, including other empirical and semi-empirical model approaches, and CFD based simulations. The main achievement is the overall model frame which can be utilized for the further development and testing of new sub-models and theories, and for concentrating the knowledge gathered from the experimental work carried out at bench scale, pilot scale and industrial scale apparatus, and from the computational work performed by other modelling methods.
机译:本文提出了一个三维半经验稳态模型,用于模拟循环流化床(CFB)过程中的燃烧,气化和排放物形成。在大型CFB炉中,燃料,空气和其他输入物料的局部进料以及不同反应物的有限混合速率会产生不均匀的工艺条件。为了模拟实际条件,应该对熔炉进行三维建模,或者应考虑三维效果。三维模拟大型CFB炉的唯一可用方法是半经验模型,该模型使用相对粗略的计算网格以及基本守恒方程,理论模型和经验相关性的组合。这种模型的数量非常少。这项工作的主要目的是建立一个模型,该模型可用于计算工业规模CFB锅炉,并且可以模拟所有基本的子现象:流体动力学,反应,颗粒磨损和传热。工作的核心是开发用于确定燃烧和吸附剂反应的模型框架和所需的子模型。达到了目标,开发的模型成功地用于研究燃烧不同类型燃料的各种工业规模CFB锅炉。吸附剂反应模型(包括钙石灰石的主要反应)用于研究在氧气燃烧中可能发生的新现象。提出的燃烧和吸附剂模型和原理也可以在其他模型方法中使用,包括其他经验和半经验模型方法以及基于CFD的模拟。主要成就是总体模型框架,该框架可用于进一步开发和测试新的子模型和理论,以及集中从在台式规模,中试规模和工业规模仪器上进行的实验工作中收集的知识,以及从其他建模方法执行的计算工作中得出。

著录项

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    Myöhänen Kari;

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  • 年度 2011
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  • 原文格式 PDF
  • 正文语种 en
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