Cynthia
Richard
a,
Armaghan
Fakhfouri
a,
Melanie
Colditz
a,
Friedrich
Striggow
a,
Romy
Kronstein-Wiedemann
b,
Torsten
Tonn
b,
Mariana
Medina-Sánchez
a,
Oliver G.
Schmidt
a,
Thomas
Gemming
a and
Andreas
Winkler
*a
aLeibniz-IFW Dresden, Helmholtzstr. 20, 01069 Dresden, Germany. E-mail: a.winkler@ifw-dresden.de
bExperimentelle Transfusionsmedizin, Medizinische Fakultät Carl Gustav Carus der Technischen Universität Dresden/DRK-Blutspendedienst Nord-Ost gGmbH, Blasewitzer str. 68/70, 01370 Dresden, Germany
First published on 14th November 2019
The ability to separate specific biological components from cell suspensions is indispensable for liquid biopsies, and for personalized diagnostics and therapy. This paper describes an advanced surface acoustic wave (SAW) based device designed for the enrichment of platelets (PLTs) from a dispersion of PLTs and red blood cells (RBCs) at whole blood concentrations, opening new possibilities for diverse applications involving cell manipulation with high throughput. The device is made of patterned SU-8 photoresist that is lithographically defined on the wafer scale with a new proposed methodology. The blood cells are initially focused and subsequently separated by an acoustic radiation force (ARF) applied through standing SAWs (SSAWs). By means of flow cytometric analysis, the PLT concentration factor was found to be 7.7, and it was proven that the PLTs maintain their initial state. A substantially higher cell throughput and considerably lower applied powers than comparable devices from literature were achieved. In addition, fully coupled 3D numerical simulations based on SAW wave field measurements were carried out to anticipate the coupling of the wave field into the fluid, and to obtain the resulting pressure field. A comparison to the acoustically simpler case of PDMS channel walls is given. The simulated results show an ideal match to the experimental observations and offer the first insights into the acoustic behavior of SU-8 as channel wall material. The proposed device is compatible with current (Lab-on-a-Chip) microfabrication techniques allowing for mass-scale, reproducible chip manufacturing which is crucial to push the technology from lab-based to real-world applications.
Existing diagnostic technologies for blood samples employ cell counting (Coulter principle),5 erythrocyte sedimentation (ESR),6 enzyme-linked immunosorbent assay (ELISA),7 polymerase chain reaction (PCR)8 and mass spectrometry (MS).9 These methods rely on accurate sample purification and pre-treatment, are time consuming and labor intensive, and are restricted to laboratory use which can be rather costly.10 Furthermore, many of these technologies are not sufficiently sensitive for low biomarker concentrations. Thus, more robust, sensitive and rapid technologies are required for blood cell separation, plasma extraction and diagnostics. Current acoustofluidic technologies, such as SAW-based actuators, have been gaining a lot of interest in medical technology owing to their biocompatibility,11 their straightforward implementation in other chip-based microfluidic techniques, and their ability to manipulate cells in a label-free and contactless manner.12–14 In addition, such devices are attractive for rapid point-of-care testing since whole blood can be directly used without the need for any pre-treatment steps.15 Acoustofluidic devices have already been used in a variety of particle and cell manipulation applications such as focusing,16,17 patterning,18–20 separation,21,22 and particularly for RBCs and PLTs separation.23 However, typical SAW-based devices demonstrated in lab environments employ microchannels fabricated via cast-molding of polydimethylsiloxane (PDMS), a tedious and rather inefficient fabrication process. PDMS remains difficult and expensive to integrate in commercially produced microfluidic devices owing to long curing times, bonding inconsistencies, and alignment issues. Moreover, there is a potentially undesirable gas and solvent permeability and absorption/adsorption inherent to this silicone polymer as well as a low chemical and mechanical stability.
In order to proceed from lab-based to real-world applications, reproducible, accurate and more efficient methods for on-chip microchannel structuring are required. There is therefore a trend in the more general field of microfluidics to move towards materials that can be used to lithographically define channels directly on top of the active microfluidic chips, such as photoresists. One of the most commonly used, and best characterized photoresists for microtechnology is the epoxy-based, negative spin-on resist, SU-8.24 It offers significant potential for microfluidic systems where the channel elements can be reliably positioned with chip-wide, micron-scale accuracy, eliminating the need for substrate bonding. Due to its straight forward microfabrication process, which is congruent to mass-scale manufacturing in the micro-electronics industry,25 it enables easy on-chip integration and is therefore a favorable alternative to PDMS in acoustofluidic applications. On the other hand, the acoustic behavior of PDMS is well characterized and its specific acoustic impedance (1.04 MPa s m−1),26 below that of water (1.48 MPa s m−1 at 25 °C),26 minimizes interfering resonances due to reduced acoustic reflections. Although a change in channel wall material would be beneficial regarding technological needs, typical polymers, glasses and metals have a higher acoustic impedance (e.g. impedance of SU-8 is 3.59 MPa s m−1) than that of water, resulting in a more complex acoustic behavior due to increased reflections at the fluid–solid interface.26,27 Thus, the channel walls and the properties of the wall material must be taken into consideration when planning the geometry of the channel layout, and for the task specific design of the SAW-chip.
To date, few publications mention SU-8 microchannels in combination with SAW.28–32 From these, only Mu et al.30 used an approach similar to the one shown here. They created SU-8 microfluidic channels with large wall widths, for SAW-based particle concentration where PDMS was used as a cover with in- and outlet openings only. The authors demonstrated a narrowing of the particle stream in their SU-8 device in comparison to results previously reported, but no cell sorting was demonstrated. In our work, an analogous device is further optimized to be more power efficient and to produce less parasitic heat by viscous attenuation of SAWs in comparison to the device introduced by Mu et al. The more complex task of cell focusing and separating was successfully accomplished for the first time in such a setup. Also, optical lithography was used to create thin, open microfluidic channels out of SU-8 directly onto 4′′ wafers. A PDMS cover was used to seal the SU-8 microchannel resulting in an exceptional platform for acoustic enrichment of PLTs with a higher separation efficiency, substantially higher cell throughput and significantly lower applied powers to current state-of-the-art. The separated platelets and red blood cells were collected at different outlets to perform platelet activation test and flow cytometry. Furthermore, a comprehensive analysis of the wave field generated on the chip surface and inside the microfluidic channel was performed. Using a fully coupled finite element method (FEM) simulation, for the first time, we demonstrate the influence of SU-8 side walls on the acoustic wave field within the fluid-filled microchannel, with excellent agreement to the experimental observations.
The interference of the opposing incident longitudinal waves subsequently forms a standing wave field inside the fluid-filled channel. Amplitude distributions of the resultant pressure field in the channel, however, are strongly affected by several features. Firstly, the longitudinal waves are reflected at the liquid/SU-8 interface due to the large difference in the acoustic impedance of SU-8 and water. Secondly, in contrast to PDMS, SU-8 has a higher acoustic impedance and a lower acoustic absorption. As follows, longitudinal waves are likely excited within the SU-8 walls, caused by acoustic refraction at the LiNbO3/SU-8 interface, leading to additional longitudinal waves radiating from the channel walls into the fluid (Fig. 2(a), inset).
The presence of a cell within this pressure field, in the fluid domain, gives rise to the acoustic radiation force (ARF), leading to the migration of cells towards certain pressure regions.33–36 The acoustic contrast factor, ϕ, a function of density and compressibility of the medium and of the cell, indicates whether the cell will be attracted to a pressure node (+ϕ) or to a pressure anti-node (−ϕ).37 Since the value of ϕ for RBCs and PLTs in a phosphate-buffered saline (PBS) solution (ρ = 1004 kg m−3, c = 1508.2 m s−1, β = 1/ρc2)38 was calculated to be 0.35 and 0.21,15 respectively, these cells will be trapped in pressure nodes. Furthermore, a cell exposed to the SSAW field in this system is also subjected to a viscous drag force induced by the fluid flow. Size-based cell separation is possible considering that the ARF and the drag force are proportional to the cell radius (FARF ∼ R3, FDrag ∼ R, where R is the cell radius).39 As such, the cell response is dictated by the dominance of these two forces (ARF and dragforce) and larger cells, for instance RBCs, will be more affected by the ARF and thus will move towards pressure nodes faster than smaller cells.
The first stage of the device (Fig. 1(a)) focuses all cells into a central pressure node, whereas separation takes place at the second stage. Here, larger cells (RBCs) will experience a larger radiation force and will therefore move towards pressure-nodes created near the channel walls faster than smaller cells (PLTs), which will remain in the center of the channel and continue along the flow.
The microfluidic channel consists of three inlets and three outlets on both ends of a larger central channel (see Fig. S1† for the overview of the chip layout). The blood sample is injected through the central inlet and a two-sided sheath flow is applied via the adjacent channels (Fig. 1(a)). The sheath flow ensures that the cells are initially located in the central channel region and experience an acoustic radiation force only towards the center nodal-region. The flow rates of the blood sample mixture and of the sheath flow were all set to 0.5 μL min−1, resulting in a total flow rate of 1.5 μL min−1 (2.7 × 106 cells per min) in the main channel. Fig. 1(c) shows the blood sample flowing through all three of the outlets when no SAW is applied. For optimal cell separation, a power of 150 mW at a driving frequency of 13 MHz was applied to the first pair of IDTs for cell focusing, and a power of 120 mW at a driving frequency of 12.7 MHz was applied to the second pair of IDTs for cell separation. In the second stage, it can be seen that the RBCs become trapped in pressure nodes created near the channel walls and are thus directed towards the upper and lower outlets. The PLTs remain in the central region and exit through the central outlet (Fig. 1(d), see also Movies S1 to S4†).
Flow cytometric analysis was performed on the collected samples and the purity of cells at each individual outlet was measured through platelet labelling. The separation efficiency, given as the ratio of the target cell purity at the desired outlet to the total number of target cells collected at all outlets, was found to be 86% for the PLTs and 77% for the RBCs. In addition, the concentration factor was calculated as the ratio of purity of desired cells at the desired outlet to the total number of these cells found in the original sample solution. It was found that the PLTs were concentrated at the middle outlet with a factor of 7.7 (an increase from 5.5% cell concentration in the original sample solution to 42.9% in the collected sample). Further optimization of the outlet channel geometry based on the current setup is expected to lead to an increase in separation efficiency and purity of the separated samples. The optimization may especially include the change of channel width ratio between outer and central channels (to adjust pressure loss), as well as the angle of the outer channels (to reduce shear forces at the trifurcation point). In addition, due to the high concentration of RBCs used in the experiment, an overflow effect was observed due to a lack of space in the central outlet. Increasing the cross-sectional area of the center outlet would thus eliminate the overflowing of RBCs into the neighbouring outlets and increase the separation efficiency of the device. To verify that little to no shear-induced stress was applied by the SSAW to the cells, the PLT activation was measured through the use of the antibody CD62P-PE (BD Bio-sciences, USA). An activation comparable to fresh blood samples was observed; deformation and coagulation of the cells did not occur. Considering that RBCs are much less sensitive to shear-stress than PLTs, they are expected to remain unaffected.
Furthermore, FEM simulations demonstrating the spatial variation in the acoustic radiation forces (x and z components both normalized by the maximum force) experienced by particles (here used as a substitution for the cells) placed in a sound pressure field were also conducted for both stages of the device (Fig. 2(d) and (e)). The forces are determined by moving the particles to various locations across a defined line of interest that cuts through the pressure nodes and anti-nodes along the channel width, with a step size of 5 μm (λSAW/60). At the focusing stage, there is a stable trapping location at x = 75 μm (λSAW/4) where the x and z components of the force are zero for both particle sizes of 3 μm and 7 μm. As a result, both particle sizes are trapped in this location; focusing occurs. At the separation stage, the larger particles experience a higher force amplitude (x-component), compared to the smaller particles, at the central region and will migrate to the neighboring pressure nodes near the channel walls. Here, the applied power is adjusted to allow for migration of larger particles (akin to RBCs) whilst preventing migration of smaller particles (akin to PLTs) to the side walls.
At the second stage, where no phase shift is present between the two TSAWs, two pressure nodes are established near the channel walls (Fig. 2(c), see also Movie S5†). From the simulations, the extent of the pressure node regions, as well as the spacing between them, were measured and compared to those of the separated blood streams obtained experimentally (Fig. S5†). The accordance of the obtained results verify the accuracy of the predictions made through the simulations. At the first stage however, the width of the focused blood stream measured experimentally extends slightly into the higher pressure region in contrast to the numerical simulation. This is assumed to be caused by a high concentration of RBCs.
For comparison, a simulation with PDMS as the channel wall material was also completed (Fig. S4†) to demonstrate the strong effects that the SU-8 properties have on the wave field. It was found that the Rayleigh angle of PDMS is 15.6° whereas that of SU-8 is 50°. This means that in the case of SU-8 the incident SAW which radiates a longitudinal pressure wave in the outer SU-8 wall will be refracted, and will be transmitted into the fluid at the SU-8/fluid interface (Fig. 2(a), inset). The effects of the additional transmitted and reflected waves in the case of SU-8 is easily visible when comparing the wave field in the LiNbO3 substrate and in the fluid filled channel. In most studies published, the walls are conventionally neglected for the case of PDMS, however, for SU-8 this cannot be done due its more complex acoustic behaviour. As such, the lateral and vertical position of the pressure nodes is dependent on the acoustic boundary condition.
For the application demonstrated here, PDMS is a suitable cover material. However, if an application requires a more chemically stable cover layer, or if gas and solvent permeability has to be reduced, either a change of cover layer material towards a more chemically stable, flexible polymer, e.g. perfluor-natural rubber (FFKM/FFPM), or a chemically-compatible coating of the inner channel wall (e.g. via synthesis of SiO2 from solution), may be possible and compatible with the presented approach.
The chips have a simple interface to the signal and fluid peripheral sources, allowing for their future integration onto point-of-care devices. Moreover, they can be used as consumables, which is an important feature, e.g. to avoid cross-contamination of analyzed blood samples. The fully-coupled 3D simulations considering the absolute pressure field in the fluidic microchannel offer insight into the acoustic phenomena that gives rise to cell manipulation. Furthermore, they highlight the significant influence the different material properties of SU-8 in comparison to PDMS as the channel wall material, have on the acoustic behavior of the proposed technology.
The excellent material properties of SU-8 combined with thin channel wall widths, and refined IDT layouts with lower losses, allow for effective SAW excitation with low applied powers. For instance, Jo et al. employed powers up to, and sometimes exceeding, 1 W, in a PDMS device for the separation of particles with similar sizes to blood cells (with flow rates from 1 μL min−1 to 8 μL min−1, however with undetermined separation efficiencies).40 In their SU-8 channel, Mu et al. used flow rates of 4 μL min−1, and 4 μL min−1 to 12 μL min−1 for the blood sample and sheath flows, respectively, with a driving power of 3 W for particle concentrating.30 A high power was required in their device due to very wide channel walls, in comparison to the approach reported here where a maximum of 150 mW was needed. They reported the isolation of exosomes from an extracellular vesicle mixture with a purity of 98.4%, and a blood cell removal rate of 99.999%. The SAW-based separation of particles, or cells, with power levels comparable to the device presented here has not yet been reported in literature. Furthermore, a lower sheath flow rate, which leads to a less diluted sample, and therefore to a higher cell throughput is reported here. For instance in their device, Nam et al., separated white blood cells (WBCs) and RBCs from PLTs in a PDMS device with a separation efficiency of 99.9% and 74.1%, respectively, but with highly diluted samples (5 μL min−1 of sheath flow and 0.25 μL min−1 of the sample resulting in the overall throughput of 1.62 × 106 cells per min) due to a much higher sheath flow.41 Even with lower applied powers and a high cell throughput, high separation efficiencies were still achieved.
This work focused on the development of a novel, SU-8-based SSAW device for high throughput enrichment of blood platelets at whole blood concentrations, although this approach is not limited to blood applications. The high separation efficiency and purity achieved in this device could also improve separation performance in other applications (cell washing, bacteria separation, etc.). Moreover, no significant shear-induced stress from the SSAW field was applied to the cells, as indicated by the low platelet activation in the flow cytometer, and is therefore harmless to the viability of blood cells as well as to comparable cell types. Conclusively, our technological approach and the realized device are versatile and can be taken from lab-based applications to real-world applications for future point-of-care diagnostics and therapeutics or for integration onto Lab-on-a-Chip platforms (Fig. 3).
Once all the structures were completed, the wafer was mounted to a dicing foil and spin-coated with a protective resist layer for dicing of individual chips (150 μm wide blade, DAD3220, Disco Corp., Japan), followed by chip cleaning. For sealing of the SU-8 microchannels, a 5 mm thick rectangular PDMS block with cut-outs above the IDT locations and punched inlet-/outlet-openings, was created using a CNC milled aluminum mold and a standard PDMS mixture (Sylgard 184, Dow Corning Corporation) at a ratio of 10:
1 by weight.
The bottom surface of the SU-8 side walls, and the fluid domain, were coupled to LiNbO3 (500 μm thick) allowing for (i) transmission of the waves into the a fluid and (ii) effects arising from transmission and amplitude decay of the SAW through the walls to the fluid. To accurately capture the physics, a distributed mapped mesh with a highly fine mesh (minimum mesh size (h value) is 1.5 × 10−5 μm) near the interfaces, was used. The complete mesh comprises 215400 domain elements, 52
420 boundary elements and 3640 edge elements. The number of degrees of freedom solved for was 4
937
853.
The key to the cell separator device represented here, is the difference in the force fields experienced by cells of different types and dimensions. To demonstrate the proposed concept, a simplified semi 3D frequency-domain FEM simulation was developed. Continuity boundary conditions were imposed on the front and back sides of the fluidic volume (x–z plane), mimicking the continuous channel used experimentally. Furthermore, matched impedance boundary conditions were used to avoid multiple reflections at the interfaces. Having imposed the conditions required to generate a representative time-averaged standing pressure field, the resultant radiation force induced on compressible PS particles (of similar size to the cells) was calculated using:43,44
![]() | (1) |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c9lc00804g |
This journal is © The Royal Society of Chemistry 2019 |