Francisco J. Galindo-Rosales*a,
Mónica S. N. Oliveirab and
Manuel A. Alvesa
aCentro de Estudos de Fenómenos de Transporte (CEFT), Departamento de Engenharia Química, Faculdade de Engenharia da Universidade do Porto, Rua Dr Roberto Frias s/n, 4200-465 Porto, Portugal. E-mail: galindo@fe.up.pt; curro@galindorosales.com; Fax: +351 22508 1440; Tel: +351 22508 1079
bJames Weir Fluids Laboratory, Department of Mechanical and Aerospace Engineering, University of Strathclyde, Glasgow G1 1XJ, United Kingdom
First published on 6th January 2014
Microfluidic cross-slot devices can generate wide regions of vorticity-free strong extensional flow near the stagnation point, resulting in large extensional deformation and orientation of the microstructure of complex fluids, with possible applications in extensional rheometry and hydrodynamic stretching of single cells or molecules. Standard cross-slot devices, with sharp or rounded corners, generate a flow field with a non-homogeneous extension rate that peaks at the stagnation point, but decays significantly with distance from the stagnation point. To circumvent this limitation, an optimized shape cross-slot extensional rheometer (OSCER) was designed numerically and shown to generate constant extension rate over a wide region of the in- and out-flowing symmetry planes [Haward et al., Phys. Rev. Lett., 2012, 109, 128301]. Since the OSCER device was based on a 2D flow approximation, the practical implementation requires a large aspect ratio, which cannot be reproduced by standard soft-lithography techniques. Here, we propose a set of new designs for optimized cross-slot geometries, considering aspect ratios of order 1 and different lengths of the homogeneous inlet/outlet-flow regions. Micro-particle image velocimetry experiments were carried out in order to validate the flow kinematics, and the velocity profiles were found to be linear along the in- and outflow centrelines in good quantitative agreement with the numerical predictions.
Despite its intrinsic potential, the standard cross-slot geometry is only able to generate a uniform extension rate in a short region near the stagnation point.6 To circumvent this limitation and provide a geometry with homogeneous extensional flow along a wide region near the stagnation point, Haward et al.24 investigated an optimized shape cross-slot extensional rheometer (OSCER), with a geometrical shape determined using the numerical optimization scheme developed by Alves.25 The OSCER device requires an aspect ratio (H/W) of order 10 or above, to generate an approximately two-dimensional (2D) flow that provides a nominally constant extension rate over a spatial domain of about 15 times the width (W) of its arms. Precisely, because the OSCER device is based on a 2D flow approximation, when fabricated in poly(dimethylsiloxane) (PDMS) by soft lithography techniques that limit the aspect ratio of the channel to moderate values, the influence of the end-walls distort the flow field and the OSCER-shaped device is not able to generate a uniform well-defined extension rate inside the cross-chamber, preventing its use by a wider community that fabricates low aspect ratio microchannels in PDMS.26,27 We present here a new set of optimized cross-slot microdevices considering aspect ratios (AR) of order 1, namely AR = 0.5, 1 and 2. Because the flow is three-dimensional in such devices, hereafter we refer to them as optimized 3D cross-slot microchannels. These designs were fabricated in PDMS by replica mould technique, and the resulting hydrodynamics was validated by means of micro-particle image velocimetry (μPIV) experiments carried out over a wide range of Reynolds number (Re ∈ [10−2, 102]) and compared with those obtained for the standard cross-slot and an OSCER-shaped device, both fabricated in PDMS with AR = 1.
This process is repeated for a number of design variable parameters, supplied by the optimizer, until the optimal shape is found. Due to the symmetry of the flow geometry, only the first quadrant of the cross-slot geometry is optimized, and the remaining walls are obtained assuming geometrical symmetry. The initial estimate used corresponds to a rounded cross-slot geometry with a characteristic radius R. The CFD flow solver is a finite-volume code developed for simulation of laminar flows of viscoelastic fluids described by differential-type constitutive equations. The numerical technique is described in detail in the works of Oliveira et al.28 and Oliveira et al.31 The governing equations are those expressing conservation of mass of an incompressible Newtonian fluid, ∇·u = 0, and the momentum equation, , with
representing the material derivative of u, ρ is the fluid density, t is the time, p is the pressure and μ is the dynamic viscosity of the fluid. Creeping flow (Stokes flow) conditions are obtained by neglecting the material derivative term in the left hand side of the momentum equation.
In this work, we have optimized seven different cross-slot microchannels, based on three geometric parameters (Fig. 1): the radius (R) of the rounded cross-slot geometry used as initial guess, the length where an uniform extension rate (Lext) is required along the centrelines and the aspect ratio of the microchannel (AR = H/W). All the geometries are defined in Table 1, where H represents the channel depth and W the inlet/outlet channel widths.† Thus, for instance, the geometry named as L2R2.5AR1 has been optimized for a value of Lext = 2W, a radius R = 2.5(W/2) and for an aspect ratio of H/W = 1.
3D optimized cross-slot | H [μm] | W [μm] | Lext [μm] | R [μm] |
---|---|---|---|---|
(a) L2R2.5AR1 | 100 | 100 | 200 | 125 |
(b) L3R4AR1 | 100 | 100 | 300 | 200 |
(c) L5R6AR1 | 100 | 100 | 500 | 300 |
(d) L5R8AR0.5 | 50 | 100 | 500 | 400 |
(e) L5R8AR1 | 100 | 100 | 500 | 400 |
(f) L5R8AR2 | 200 | 100 | 500 | 400 |
(g) L10R10AR1 | 100 | 100 | 1000 | 500 |
(h) Standard | 100 | 100 | ∼150 | — |
(i) OSCER-shaped | 100 | 100 | 1500 | 1000 |
Fig. 2 shows the normalized velocity profiles (uy/U) along the vertical (outflow) centreline at different z-planes, where U is the average velocity in the inlet/outlet channels, and the corresponding extension rate () profiles resulting from the 3D optimization of cross-slot microchannel using a Newtonian fluid under creeping flow conditions. These profiles follow the expected target functions closely, with a linear variation of the velocity profile in the region of envisaged constant strain-rate and showing sharp transitions at the end of this defined zone of constant extension rate, thus providing an excellent control of the extension rate to which the fluid or the object being analysed is subjected to in the central cross chamber of the device. However, there is a clear gradient of extension rate in the z-direction (along depth), with the strain-rate reaching its maximum value at the mid-plane and decreasing towards the bottom/top walls as a direct consequence of the no-slip condition at the end-walls. Despite this strain-rate gradient, we should highlight that the uniformity of the extension rate profiles at each z-plane is maintained. The non-negligible gradient of extension rate along the depth of the channel may limit somehow the applicability of these 3D optimized cross-slot devices for extensional microfluidic rheometry, since it can have repercussions on the extra pressure drop, as well as on flow induced birefringence measurements, which rely on a cumulative measurement of the retardation throughout the light path (depth of the channel). However, we note that near the centreplane the variation of the strain-rate with the depth is moderate, as illustrated in Fig. 2(b). For the profiles at z/(H/2) = 0.2 and z/(H/2) = 0.4, a variation of 20% and 40% along z corresponds to a variation of 3.7% and 14%, respectively, in the strain-rate with regards to the centreplane (z/(H/2) = 0). In the particular case of applications involving the stretching of single macromolecules or cells, because these specimens can be trapped in the central region of the cross chamber at the mid-plane, the uniformity of the extension profiles around the mid-plane generated by these 3D optimized cross-slots is a promising leap forward towards the mechanical characterisation of molecules and cells in lab-on-a-chip devices under well controlled homogeneous extensional flow conditions.
![]() | ||
Fig. 3 Scanning electron microscopy (SEM) images of the cross-slots used in this work as described in Table 1. In cases (a)–(h) a top-view is shown, while in case (i) a perspective view is illustrated. |
The experimental results presented here were obtained using distilled water as working fluid. All the experiments were carried out at an average temperature of 295 K, for which the dynamic viscosity and the density of distilled water are μ = 0.96 mPa s and ρ = 997.8 kg m−3, respectively.
The flow in the cross chamber was characterized experimentally using μPIV32,33 following the procedure detailed by Oliveira et al.34 A CCD camera (FlowSense 4M camera, Dantec Dynamics) connected to an inverted microscope (Leica DMI 5000 M) with 10× and 20× objective lenses (numerical aperture, NA = 0.30 and NA = 0.5, respectively) and a filter cube were used to acquire the images in the mid-plane (z = 0). For volume illumination of the flow, we used a double-pulsed Nd:YAG laser system operating at a wavelength of λ = 532 nm. As tracer particles, we used 1 μm diameter fluorescent particles (FluoSphere carboxylate-modified, nile red, Ex/Em = 535/575 nm) at a concentration of ∼0.02% by volume. The time lapse between two consecutive frames was adjusted depending on the flow rate. For all cases, a minimum of 100 image pairs were recorded, divided into interrogation areas of 32 × 32 pixels. These images were processed and ensemble averaged using the DynamicStudio software (version 2.30.47, Dantec Dynamics).
The flow rate was controlled by means of a neMESYS low pressure syringe pump (Cetoni GmbH) with three independent modules. The flow rates considered ranged from 2 μl h−1 to 36 ml h−1 in order to cover Reynolds numbers from 10−2 up to 102 in all the geometries. Depending on the flow rate different Hamilton syringes (25 μl, 500 μl and 1 ml) were used to ensure pulsation-free dosing. Three pumps controlled two inlet and one outlet flow rates, while the remaining outlet was left open to the atmosphere to balance the flow.
As the optimization was carried out for creeping flow conditions, the uniformity of the strain-rate profiles and the length of uniform extension is only close to expected values at low Re. When the flow conditions deviate significantly from inertialess flow conditions the strain-rate field becomes less homogeneous (Re ≳ 10), even for the channels with the largest aspect ratio as shown in Fig. 5. This does not mean that it is impossible to achieve a uniform extension rate at higher values of Re, but instead it requires the optimization of a new geometry taking into account the convective terms in the momentum equation. However, it is not practical to have different geometries for different values of Re and therefore we have restricted our analysis to low Re, since these conditions are easily met and are relevant for microfluidics.
Fig. 6(a) shows a comparison between the normalized velocity profiles measured for the 3D optimized cross-slot microdevices, the OSCER-shaped device and the standard cross-slot. At AR = 1, the OSCER-shaped device and the standard cross-slot are clearly not as effective in obtaining a homogeneous flow field along the outlet centrelines, while the velocity profiles in the extension dominated region are clearly linear for all the optimized devices and the region of uniform extension rate for each one has the predicted length. As a consequence, playing with the flow rate (Q) and the length of the extension region (Lext), it is possible to reach whichever position in the − Re parameter space (Fig. 6(b)) required, as long as Re is low (Re ≲ 10). Thus, with our optimal shape design approach it is possible to create a 3D optimized cross-slot device on demand depending on the requirements for controlled extensional flow.
Footnote |
† Electronic supplementary information (ESI) available: As an example, the profiles of the geometries L5R8AR0.5, L5R8AR1 and L5R8AR2 are provided. See DOI: 10.1039/c3ra47230b |
This journal is © The Royal Society of Chemistry 2014 |