超大尺度微流体网络中物种迁移的简化模型

A. Taher, B. Jones, P. Peumans, L. Lagae
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引用次数: 0

摘要

提出了一种新的模拟超大规模微流体网络中流体流动和物质输运的方法,并将其应用于大规模并行微反应器。微流控电路的大规模集成(VLSI)为许多生物测试应用提供了一个有吸引力的解决方案,如基因表达、DNA测序和药物筛选,这些应用需要大规模的并行化反应来提高通量和减少获得结果的时间。然而,由于需要大量的计算资源,VLSI微流体的设计和建模仍然具有传统的2D或3D计算流体动力学(CFD)技术的挑战性。使用简化模型对于减少现有计算资源上的模拟时间至关重要。许多微流控网络可以用类似电路的基于电阻的网络来解决;然而,微流控网络中物质输运(扩散+平流)的简化模型却很少受到关注。本文介绍了一种基于阻力网络的流动动力学简化模型,并将其与平流扩散输运方程的一维离散化相结合。利用ANSYS Fluent对一个由4 × 4微反应器组成的流动网络进行了CFD仿真验证。对于长宽比为10的通道,计算结果与二维CFD模拟结果吻合较好,总压降误差小于6%。当通道长宽比为20时,误差仅为3%。然后将开发的模型用于优化设计用于高纯度试剂循环加载的100个微反应器网络。用该程序对反应器配置进行了计算,计算了最小的试剂装卸周期时间和最小的操作压力。理论上,在进一步优化代码并利用并行处理后,模拟可以扩展到更大的反应堆阵列。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A Simplified Model for Species Transport in Very Large Scale Microfluidic Networks
A novel modeling technique for fluid flow and species transport in very large scale microfluidic networks is developed with applications to massively parallelized microreactors. Very large scale integration (VLSI) of microfluidic circuits presents an attractive solution for many biological testing applications such as gene expression, DNA sequencing and drug screening, which require massive parallelization of reactions to increase throughput and decrease time-to-result. However, the design and modeling of VLSI microfluidics remains challenging with conventional 2D or 3D computational fluid dynamic (CFD) techniques due to the large computational resources required. Using simplified models is crucial to reduce simulation time on existing computational resources. Many microfluidic networks can be solved using resistance based networks similar to electrical circuits; however, simplified models for species transport (diffusion plus advection) in microfluidic networks has received much less attention. Here, we introduce a simplified model based on resistance network based modeling for flow dynamics and couple it with a one-dimensional discretization of the advection-diffusion transport equation. The developed model was validated against CFD simulations using ANSYS Fluent for a flow network consisting of a 4 by 4 array of microreactors. It showed good agreement with 2D CFD simulations with less than 6% error in total pressure drop across the network for channels with a length to width ratio of 10. The error was only 3% for a channel length to width ratio of 20. The developed model was then used to optimize the design of a 100-microreactors network used for high purity cyclical loading of reagents. The reactor configuration with a minimum cycle time for reagent loading and unloading and minimum operating pressure were evaluated with the code. In theory, the simulation can be scaled to much larger reactor arrays after further optimizations of the code and utilizing parallel processing.
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