3. Results and Discussion
A silicon microdevice with recurring sharp corners on the channel side wall of 30º was made to evaluate whether this structure has benefits over a regular straight channel. All the devices in this study were etched in silicon substrates and were made by a Bosch process from the Deep Reactive Dry Etching (DRIE) category.
Figure 2 shows a SEM image of the device; as is evident from the images, the sharp edges turned out to be of different sizes and different continual consistency. In DRIE, high aspect ratios (AR, depth to width ratio) and smaller feature sizes increase the difficulty of maintaining sharp profiles. The etching uniformity control decreases as the AR increases, leading to more pronounced scalloping and less sharp features [
19]. On the other hand, the isotropic etching phase of the Bosch process is characterized by less directional ion bombardment, which does not discriminate between horizontal and vertical surfaces. This non-selectivity can lead to lateral etching under the mask, resulting in rounded or sloped profiles rather than sharp, defined edges [
20].
The channel width of these microchips was chosen based on the standing wave criterion of BAWs. This means that at 2 MHz resonance frequency (PZT thickness:1 mm), in water, the sound velocity equals 1.5×10
3 m/s, corresponding to a wavelength of 750 µm. Based on this indication, at 2 MHz resonance frequency, one pressure node forms in the 375 µm channel. However, when introducing the sharp corners to the channel, determining which PZT transducer and frequency were optimal for this microdevice is not straightforward. Therefore, to choose which PZT transducer and resonance frequency to use, four PZT transducers with different thicknesses from 0.91-1.25 mm were used to measure the average streaming (lateral flow) velocity at an applied frequency range between 1.6-2.6 MHz at 34 V. The results are shown in
Figure 3.
The results show that the best-performing PZT transducers are the 1.1 mm at 2 MHz and 1 mm at 2.2 MHz. The characterization experiments continued with the 1mm PZT transducer at 2.2 MHz frequency because of the wide availability of this PZT type in our lab.
The mixing efficiency of the microdevice with recurring 30º sharp corners was measured at 2.2 MHz with an amplitude of 170 V. The top experimental image shows the flow of water and fluorescent dye when the acoustic device is turned off, and the bottom experimental image shows the mixed fluorescent dye when the acoustic device has been turned on. The graph next to it shows the mixing index (efficiency) versus the time when the acoustic is turned on and off two consecutive times.
The results show the mixing index reaches almost 80 % within 0.2 s. The mixing rate was dramatically improved when comparing the results with those without structures on the side wall. The mixing efficiency takes around 5 s to reach 65% in the same conditions for a regular channel. Therefore, the mixing time was reduced a a factor of 25. Sharp corners or edges in microfluidic channels can intensify mixing by creating localized flow disturbances, leading to micro vortices and streaming flows. These flows enhance mixing of fluids by disrupting the typical laminar flow patterns common in microscale environments. The interaction of acoustic waves with sharp edges leads to a steady flow known as sharp-edge acoustic streaming (SEAS). This streaming can significantly enhance mixing by continuously stirring the fluids, thus reducing the mixing length and time required to achieve homogeneity [
21]. The geometry of the sharp edges, including the angle and spacing between edges, plays a crucial role in the effectiveness of mixing. Optimal sharp-edge designs can maximize the streaming velocity and the extent of the induced vortices, thereby improving the mixing efficiency [
22]. Studies have shown that the sharp-edge structures can be optimized for more effective mixing patterns. For instance, specific configurations of sharp edges where the spacing between each tip is 200-300 µm allow fluids to jump out from each sharp edge to reach zones between two consecutive edges at the opposite wall, enhancing the mixing process. Direct numerical simulations and experiments with dye visualizations have confirmed that SEAS micromixers can decrease the micromixing time significantly by optimizing the sharp-edge patterns and operating conditions [
22].
The influence of the sharp corner position on mixing has also been investigated, showing that the placement and design of these corners can be crucial for achieving efficient mixing in microfluidic devices [
13].
When comparing the velocity vector sizes shown in the two images next to one another in
Figure 5, it is clear that acoustic streaming of sharp-edged structures increases by increasing the voltage applied to piezoelectric transducers that generate acoustic waves. Higher amplitudes lead to increased acoustic streaming flows around sharp edges, evident by the size of velocity vectors in the figure, which is crucial for enhancing mixing in silicon devices. The increase in streaming velocity with higher voltages is due to the more significant energy input into the system, which improves the amplitude of acoustic vibrations. These stronger vibrations lead to more pronounced acoustic streaming effects, particularly around sharp edges where the flow disturbances are maximized due to the geometric singularities. It is well known that increasing the voltage from 10V to 40V significantly improves micromixing by reducing the mixing time [
22].
Although the device with 30º sharp structures showed promising results, the optimal ideal tip angle for fast mixing purposes must be evaluated in more detail. To this end, the average velocity of the streaming around sharp corners of 10º, 20º, 30º, 40º, and 60º was measured at 2.2 MHz between 9-28 Vpp. The results in
Figure 6 indicate that the best-performing tip angle for achieving fast mixing is firstly 10º and secondly 20º. These two angles can increase the streaming velocity 14 and 8 times, respectively, compared to a channel with the same width and depth lacking sharp corners (Refer to SI video S3). Beyond these two angles, the average velocity decreased drastically. Still, the average velocity beyond 20º and until 60º is 1.5 times faster than in the same conditions and channel only without the sharp-edged structures. In a study on PDMS-based microdevices, four different tip angles of 15°, 30°, 45°, and 60° were investigated to determine the optimal angle for the best acoustic streaming effect and mixing performance. The results demonstrated that rapid and homogeneous mixing could be achieved by optimizing the design of the sharp edges. 15º showed fast, excellent mixing, while 30º mixing results and mixing time were acceptable [
12].
Figure 6 shows the tip angle's effectivity and the positive trend of increasing the amplitude, resulting in higher streaming velocity. Due to the abrupt change in flow direction, a sharper edge induces stronger and more localized vortices. These vortices promote chaotic advection, where fluid particles mix rapidly across different streamlines. A less sharp edge still induces vortices but to a lesser extent. The smoother change in flow direction reduces the intensity and effectiveness of vortex formation, leading to less efficient mixing. Also, higher shear stress is generated with sharper tips, which enhances fluid dispersion and accelerates the mixing process. With fewer sharp corners, shear stress is lower, resulting in slower fluid dispersion and potentially leaving unmixed regions within the channel. This can lead to incomplete mixing and longer mixing times.
Other than the tip angle, another variable is the tip shape; adding more corners or edges over the tip produces extra micro-streaming lesions, increasing the streaming velocity and speeding up mixing. Four different tip shapes were produced, and 1 µm polystyrene particles were introduced into the channel. Multiple images were captured at different focal depths (z-planes), and then they were combined to produce a single image that is sharp and in focus throughout the entire depth. This so-called z-stacking of the experimental movie frames at the max intensity combined with each other shows that each tip shape reveals flow characteristics. Both the sketched design of the tip shape and an image of the produced tip shape in silicon taken with an optical microscope are included in
Figure 7.
This variation in shape and the displacement micro-streaming results in different average streaming velocities at the same amplitude. As shown in
Figure 7, some shapes have inactive areas around where no displacement is observed, which can cause those shapes not to be suited for fast mixing applications. To conclude which tip shape works best, the tip shapes were organized in
Figure 8 based on their streaming average velocity magnitude. Also, the effect of the sharp-edged structure was studied in two different areas. The blue bars are the measured average velocity in a 2.5 times bigger area than the green bars.
Figure 8 clearly shows the tips with more edges present the best performance. However, if we follow the displacement lines around the sharp tip in
Figure 7, the best performance was obtained for the tip shapes with more symmetrical displacement with no inactive area (
Figure 8. b and d). With these findings, it can be concluded that next to the tip angle of the sharp edges and the ratio h/H between the distance of the sharp edges from the wall (h) and the overall channels width (H) [
19], the shape of the tip affects the flow field as well.
The position of the sharp edges has been studied before in PDMS devices. When the sharp corners are positioned closer to one another than 100 µm, the mixing performance deteriorates [
17]. Also, with precise calculation and simulations, a silicon device was made containing two side wall sharp edges that mix, pump, and trap the particles [
11]. In this work, we tested the position of the sharp structures in the middle of the channel as a 3D structure. When the acoustic force is applied, SEAS occurs. Interestingly, after a few seconds, a unidirectional pumping effect occurs inside the channel, and the liquid inside starts pumping in one direction to the point that, within seconds, the channel is almost emptied (Please refer to the SI video S4).
Figure 9.
Z-stacking of particle movements in the channel with triangular pillars. The top-left image shows all the frames since the start of streaming and pumping on top of one another.
Figure 9.
Z-stacking of particle movements in the channel with triangular pillars. The top-left image shows all the frames since the start of streaming and pumping on top of one another.
This result shows that by placing the sharp corners inside the channel, we create an abrupt change in the channel flow direction. Streaming around the sharp edges, its vortices, and circulations in the middle of the channel result in a net force directed to one side of the channel, and pumping occurs because the generated net forces by acoustic streaming push the bulk fluid forward. This effect can be tuned by changing the applied voltage; the higher the voltage, the less time it takes for the pumping to start following the sharp edge streaming (SI S4 and S5). Both the effect of directionality and the applied voltage on the pumping effect were done before with structures pointing in one direction at the edge of the rectangular channels in PDMS [
14], which seems to be a similar effect to what is observed in our silicon devices with sharp-edged pillars placed in the middle of the channel. Another variation of the pumping device was made but with circular 3D structures in the middle of the channel. Surprisingly, the circular and sharp-edged pillars showed the streaming around the pillars and the pumping effect (Please refer to SI video S5). However, the time needed for pumping to start was longer for circular structures compared to triangular structures at the same amplitude. This phenomenon can be explained by the fact that the sharp corner can be parallel to the transducer position (like the triangular pillar), or the sharp corner can be orthogonal to the transducer position (the circular pillar with the scallops originating from the DRIE process), which means the circular pillar also contains sharp angles like the triangular pillar but in a different position and based on their angle the vortices forms in different patterns [
23]. In our study, the channels were sealed with a glass wafer, and the scallop formation can induce the circulation and movement of liquid around the circular pillars (
Figure 10b).
Before the pumping effect starts, there are liquid movements around the pillars. The movement patterns in a channel with triangular pillars are similar to the symmetrical streaming happening around the sharp edge (
Figure 9), and the movement around the circular pillar is rotated in one direction around each pillar (
Figure 10). When the average velocity of such movements is compared with each other,
Figure 11.a shows that both movements in the channel become faster by increasing the applied voltage and that the flow patterns around the triangular pillar are faster than those around circular pillars. When the pumping effect starts, the pumping velocity increases with time (
Figure 11.b). This increase is more significant in channels with triangular pillars yet still discoverable in channels with circular pillars. The leading cause of the pumping effect is yet to be characterized and studied in more depth in a follow-up publication.