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Liter-scale production of uniform gas bubbles via parallelization of flow-focusing generators

机译:通过流动聚焦发电机的并行化升降尺寸生产均匀气泡

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摘要

Microscale gas bubbles have demonstrated enormous utility as versatile templates for the synthesis of functional materials in medicine, ultra-lightweight materials and acoustic metamaterials. In many of these applications, high uniformity of the size of the gas bubbles is critical to achieve the desired properties and functionality. While microfluidics have been used with success to create gas bubbles that have a uniformity not achievable using conventional methods, the inherently low volumetric flow rate of microfluidics has limited its use in most applications. Parallelization of liquid droplet generators, in which many droplet generators are incorporated onto a single chip, has shown great promise for the large scale production of monodisperse liquid emulsion droplets. However, the scale-up of monodisperse gas bubbles using such an approach has remained a challenge because of possible coupling between parallel bubbles generators and feedback effects from the downstream channels. In this report, we systematically investigate the effect of factors such as viscosity of the continuous phase, capillary number, and gas pressure as well as the channel uniformity on the size distribution of gas bubbles in a parallelized microfluidic device. We show that, by optimizing the flow conditions, a device with 400 parallel flow focusing generators on a footprint of 5 x 5 cm(2) can be used to generate gas bubbles with a coefficient of variation of less than 5% at a production rate of approximately 1 L h(-1). Our results suggest that the optimization of flow conditions using a device with a small number (e.g., 8) of parallel FFGs can facilitate large-scale bubble production.
机译:微观气泡已经表现为多功能模板的巨大用途,用于合成医药,超轻型材料和声学超材料中的功能材料。在许多这些应用中,气泡尺寸的高均匀性对于实现所需的性能和功能至关重要。虽然Microfluidics已经使用成功以使用常规方法产生均匀性的气泡,但微流体的固有低体积流速限制了其在大多数应用中的使用。液滴发生器的并行化,其中许多液滴发生器结合到单个芯片上,对单分散液体乳液液滴的大规模生产表示了很大的希望。然而,使用这种方法的单分散气泡的扩展仍然是挑战,因为不同于并联气泡发生器之间的可能耦合和来自下游通道的反馈效果。在本报告中,我们系统地研究了连续相,毛细管数和气体压力粘度等因素的影响以及并行化微流体装置中气泡尺寸分布的通道均匀性。我们表明,通过优化流动条件,占地面积为5×5cm(2)的占地面积的装置,可用于产生具有小于5%的气泡,以生产率小于5%大约1升H(-1)。我们的研究结果表明,使用具有较小数量(例如,8)的平行FFG的装置的流动条件可以促进大规模的泡沫产生。

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