玻璃熔炼机内多相玻璃熔体流动的模拟

S. Chang, Chenn Q. Zhou, B. Golchert, M. Petrick
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引用次数: 1

摘要

一个典型的玻璃炉由一个燃烧空间和一个熔炼机组成。燃烧空间中燃料和空气/氧气燃烧产生的强烈热量主要通过辐射传递到熔化机,熔化砂和碎玻璃(碎玻璃)在那里熔化,形成熔融玻璃。熔体流动是一个复杂的多相流动,包括固体砂/碎屑和熔融玻璃。正确模拟固体和液体玻璃的流动模式是决定玻璃质量和炉效率的关键。开发了一个多相CFD程序来模拟玻璃熔池流动。它对固体批次和液体玻璃熔体流动都使用欧拉方法。利用批流的质量守恒方程、动量守恒方程和能量守恒方程求解批流的局部粒子数、密度、速度和温度。以类似的方式,玻璃熔体流动的质量、动量和能量守恒方程用于求解局部液态玻璃液的压力、速度和温度。固体批次在顶部由燃烧空间的热量熔化,在下方由玻璃熔体流的热量熔化。燃烧空间的换热率采用辐射模型计算,玻璃熔体流到固体料的换热率采用基于局部颗粒数密度和玻璃熔体温度的模型计算。能量和质量在批料和玻璃熔体之间达到平衡。批覆盖率由局部粒子数、密度和速度决定。在不同的运行/设计条件下,对工业规模的玻璃熔炼机进行了模拟。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Simulation of Multi-Phase Glass-Melt Flows in a Glass Melter
A typical glass furnace consists of a combustion space and a melter. The intense heat, generated from the combustion of fuel and air/oxygen in the combustion space, is transferred mainly by radiation to the melter where the melt sand and cullet (scrap glass) are melted, creating molten glass. The melter flow is a complex multi-phase flow including solid batches of sand/cullet and molten glass. Proper modeling of the flow patterns of the solid batch and liquid glass is a key to determining the glass quality and furnace efficiency. A multi-phase CFD code has been developed to simulate glass melter flow. It uses an Eulerian approach for both the solid batch and the liquid glass-melt flows. The mass, momentum, and energy conservation equations of the batch flow are used to solve for local batch particle number density, velocity, and temperature. In a similar manner, the conservation equations of mass, momentum, and energy of the glass-melt flow are used to solve for local liquid molten glass pressure, velocity, and temperature. The solid batch is melted on the top by the heat from the combustion space and from below by heat from the glass-melt flow. The heat transfer rate from the combustion space is calculated from a radiation model calculation while the heat transfer rate from the glass-melt flow to the solid batch is calculated from a model based on local particle number density and glass-melt temperature. Energy and mass are balanced between the batch and the glass-melt. Batch coverage is determined from local particle number density and velocity. A commercial-scale glass melter has been simulated at different operating/design conditions.
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