存在内部热源时颗粒流态化数学模型的建立

A. Mitrofanov, S. Vasilevich, M. Malko, L. Ovchinnikov, N. Shpeynova
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引用次数: 0

摘要

由于从外部来源提供高温剂,用于散装介质热处理的设备被广泛使用。在这种情况下,使用流化技术,热剂也执行流化介质的功能。在某些情况下,直接在流化床中对颗粒进行欧姆加热可以被认为是一种替代和首选的技术。然而,为了有效地组织这些过程,我们需要可靠的模型来预测流化床本身的结构,因为它在很大程度上决定了导电性,因此也决定了加热的强度。流化床是一个非均匀非均质系统,因此,假设其空间离散化的数学模型对于其充分描述是必要的。因此,开发这样的模型是一项紧迫的任务。利用马尔可夫链理论的数学装置作为数学基础,对流化床中散装介质的结构进行了建模。模型的参数识别是使用文献中已知的依赖项来执行的。转移矩阵与质量流的物理参数对齐,使模型非线性化。流化床中的电热过程在定性水平上描述,假设床的代表体积的加热强度与其中颗粒的体积浓度成反比。气相传热传质过程是决定床层温度渐近的一个限制因素。本文用数值方法研究了在有内部热源的情况下,流化床的结构和膨胀对相加热强度的影响,而内部热源的强度与固相浓度成反比。估计了模型各参数对仪器内热态形成的影响。结果表明,为了适当地描述仪器中的过程,必须将其作为具有分布空间参数的对象进行分析。本文表明,马尔可夫链方法是一种可接受的工具来描述这种颗粒系统的结构,如流化床。数值实验结果与流化床理论在定性上有较好的一致性。为流化床介质欧姆加热系统的计算提供了可靠的科学依据。
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Development of mathematical model of fluidization of particles in presence of internal heat sources
Devices for heat treatment of bulk media due to the supply of high-temperature agent from an external source are widely used. In this case using the fluidization technique, the thermal agent also performs the function of a fluidizing medium. The ohmic heating of particles directly in the fluidized bed can be considered as an alternative and preferred technology in some cases. However, to organize such processes effectively we need reliable models to predict the structure of the fluidized bed itself, since it largely determines the conductivity, and, hence, the intensity of heating. The fluidized bed is an inhomogeneous heterogeneous system, therefore, mathematical models assuming its spatial discretization are necessary for its adequate description. Thus, the development of such models is an urgent task. The mathematical apparatus of the Markov chain theory is used as a mathematical basis to model the structure of a bulk medium in a fluidized bed. Parametric identification of the model is performed using the dependencies known from the literature. The transition matrices have been aligned with the physical parameters of the mass flows, which makes the proposed model nonlinear. The electrothermal process in the fluidized bed is described at a qualitative level with an assumption that the heating intensity of the representative volume of the bed is inversely proportional to the volume concentration of particles in it. The gas-particle heat and mass transfer process is a limiting factor that determine the asymptotic temperature in the bed. The authors have studied numerically the influence of the structure and expansion of the fluidized bed on the heating intensity of its phases in case we have internal heat sources, the intensity of which is inversely related to the concentration of the solid phase. The influence of various parameters of the model on the formation of the thermal regime in the apparatus is estimated. It is shown that for an appropriate description of processes in the apparatus, its analysis as an object with distributed spatial parameters is necessary. The paper shows that the methodology of the Markov chain approach is an acceptable tool to describe the structure of such particle systems as a fluidized bed. The obtained results of numerical experiments are in good qualitative agreement with the fluidized bed theory. They can be considered as a reliable scientific basis to calculate the system of ohmic heating of media in a fluidized bed.
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