Burger S, Schulz M, von Stetten F, Zengerle R, Paust N
Hahn-Schickard, Georges-Koehler-Allee 103, 79110 Freiburg, Germany.
Lab Chip. 2016 Jan 21;16(2):261-8. doi: 10.1039/c5lc01280e.
We present batch-mode mixing for centrifugal microfluidics operated at fixed rotational frequency. Gas is generated by the disk integrated decomposition of hydrogen peroxide (H2O2) to liquid water (H2O) and gaseous oxygen (O2) and inserted into a mixing chamber. There, bubbles are formed that ascent through the liquid in the artificial gravity field and lead to drag flow. Additionaly, strong buoyancy causes deformation and rupture of the gas bubbles and induces strong mixing flows in the liquids. Buoyancy driven bubble mixing is quantitatively compared to shake mode mixing, mixing by reciprocation and vortex mixing. To determine mixing efficiencies in a meaningful way, the different mixers are employed for mixing of a lysis reagent and human whole blood. Subsequently, DNA is extracted from the lysate and the amount of DNA recovered is taken as a measure for mixing efficiency. Relative to standard vortex mixing, DNA extraction based on buoyancy driven bubble mixing resulted in yields of 92 ± 8% (100 s mixing time) and 100 ± 8% (600 s) at 130g centrifugal acceleration. Shake mode mixing yields 96 ± 11% and is thus equal to buoyancy driven bubble mixing. An advantage of buoyancy driven bubble mixing is that it can be operated at fixed rotational frequency, however. The additional costs of implementing buoyancy driven bubble mixing are low since both the activation liquid and the catalyst are very low cost and no external means are required in the processing device. Furthermore, buoyancy driven bubble mixing can easily be integrated in a monolithic manner and is compatible to scalable manufacturing technologies such as injection moulding or thermoforming. We consider buoyancy driven bubble mixing an excellent alternative to shake mode mixing, in particular if the processing device is not capable of providing fast changes of rotational frequency or if the low average rotational frequency is challenging for the other integrated fluidic operations.
我们展示了在固定旋转频率下运行的离心微流控的批处理模式混合。通过过氧化氢(H2O2)分解为液态水(H2O)和气态氧(O2)的盘式集成反应产生气体,并将其插入混合腔室。在那里,形成气泡,这些气泡在人工重力场中向上穿过液体并导致曳流。此外,强大的浮力会导致气泡变形和破裂,并在液体中引发强烈的混合流。将浮力驱动的气泡混合与摇动模式混合、往复混合和涡旋混合进行了定量比较。为了以有意义的方式确定混合效率,使用不同的混合器来混合裂解试剂和人全血。随后,从裂解物中提取DNA,并将回收的DNA量作为混合效率的度量。相对于标准涡旋混合,在130g离心加速度下,基于浮力驱动的气泡混合进行DNA提取,在100秒混合时间时产率为92±8%,在600秒时产率为100±8%。摇动模式混合的产率为96±11%,因此与浮力驱动的气泡混合相当。然而,浮力驱动的气泡混合的一个优点是它可以在固定的旋转频率下运行。实施浮力驱动的气泡混合的额外成本很低,因为活化液和催化剂成本都非常低,并且处理设备不需要外部手段。此外,浮力驱动的气泡混合可以很容易地以整体方式集成,并且与注射成型或热成型等可扩展制造技术兼容。我们认为浮力驱动的气泡混合是摇动模式混合的一个极好替代方案,特别是当处理设备无法提供快速的旋转频率变化时,或者当低平均旋转频率对其他集成流体操作具有挑战性时。