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Transient Heat Transfer in a Packed-Bed Elliptic Cylindrical Reactor: A Finite-Volume Approach

机译:填充床椭圆圆柱形反应器中的瞬态传热:有限体积的方法

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This work aims to develop a transient three-dimensional mathematical model using the elliptic cylindrical coordinate system, to predict heat transfer in a elliptic cylindrical packed fixed bed reactor. The model considers variable thermo physical properties and a parabolic temperature profile at the fluid inlet. The governing equation is solved using the finite volume method. Results of temperature profile along the reactor are presented and discussed at different moments.It was verified that the maximum heat transfer rate inside the reactor occurs near the extreme region close to minor semi-axis of the ellipse; the higher temperatures at the reactor surface are also in this region, along the entire height of the bed; the steady-state regime is reached at t = 4.5 s of process, presenting after this time interval,small axial temperature gradients and high radial gradients along of the reactor bed; the parabolic temperature profile give to the bed a predominance of radial temperature gradients, and the radial porosity profile favours a higher heat transfer rate at reactor surface.
机译:该工作旨在使用椭圆圆柱坐标系开发瞬态三维数学模型,以预测椭圆圆柱形填充固定床反应器中的热传递。该模型考虑了流体入口处的可变热物理性质和抛物线温度曲线。使用有限体积法解决了控制方程。在不同的时刻介绍和讨论了沿反应器的温度曲线的结果。验证了反应器内的最大传热速率在靠近椭圆的较小半轴的极端区域附近发生;反应器表面的较高温度也在该区域中,沿着床的整个高度;在工艺T = 4.5秒达到稳态方案,在该时间间隔之后呈现,沿着反应器床的小轴向温度梯度和高径向梯度;抛物线温度曲线给床径向温度梯度的优势,并且径向孔隙率曲线在反应器表面上具有较高的传热速率。

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