基于热流体隔室模型的多通道微反应器中通道和歧管的形状设计

IF 2.5 Q3 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
O. Tonomura, M. Noda, S. Hasebe
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引用次数: 0

摘要

在微反应器的设计中,形状和尺寸是实现高性能的重要设计因素。计算流体动力学(CFD)的最新进展使我们能够在不进行实验的情况下了解不同形状和尺寸的微反应器中的流动和温度分布。然而,开发一个比CFD更简单的模型来进一步减少反应堆设计和迭代性能评估所需的计算时间往往很重要。本研究提出了一种基于热流体室模型的多通道微反应器基本设计方法。该方法包括热设计和流体设计两部分。在热设计部分,设计了两种类型的热室,用于离散被壁包围的反应通道,并描述通道上的质量和热平衡,以优化通道形状。在流体设计部分,引入了三种类型的流体室,用于离散反应器和描述反应器上的质量和压力平衡,以优化歧管形状。将该方法应用于一个设计问题,结果表明微通道和变宽度的流形分别可以有效地实现均匀的温度和流量分布。除了提出的设计方法外,还开发了一种基于传递函数的隔间模型来估计流体在微反应器中的停留时间分布,而无需运行时间相关的CFD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。
Shape design of channels and manifolds in a multichannel microreactor using thermal-fluid compartment models
In the design of microreactors, the shape as well as the size is an important design factor for achieving high performance. Recent advances in computational fluid dynamics (CFD) enable us to know flow and temperature distributions in microreactors of various shapes and sizes without conducting experiments. However, it is often important to develop a simpler model than CFD to further reduce the computational time required for reactor design with iterative performance evaluations. In this research, a thermal-fluid compartment model-based approach is proposed for basic design of a multichannel microreactor. The proposed approach consists of two parts, i.e., thermal design and fluid design. In the thermal design part, two types of thermal compartments, which are used to discretize a reaction channel surrounded by wall and describe the mass and heat balances over the channel, are developed to optimize the channel shape. In the fluid design part, three types of fluid compartments, which are used to discretize the reactor and describe the mass and pressure balances over the reactor, are introduced to optimize manifold shape. The proposed approach is applied to a design problem and the results show that microchannels and manifolds with varying width are effective in realizing the uniform temperature and flow distributions, respectively. In addition to the proposed design approach, a transfer function-based compartment model is developed to estimate the residence time distribution of fluid in a microreactor without running time-dependent CFD simulation.
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来源期刊
CiteScore
3.50
自引率
0.00%
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审稿时长
13 weeks
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