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In this report, we presented a repeatable and accessible experimental setup and protocol to adapt the Taylor dispersion experiment to the microfluidic scale. We leverage an existing xurography technique5 to manufacture our microchannels in-house at low cost using 3D-printing and a desktop craft cutter. The current industry standard for microchannel manufacturing involves the creation of master molds in which channels can be cast. Compared to the technique discussed in this manuscript, these methods can have significantly better channel resolution and feature size (some as small as 0.1 µm), but have the drawback of much higher overhead costs, up to tens of thousands of USD14. In addition to the initial overhead cost, any change to channel design features requires both the creation of a new master mold and the curing of new channels, increasing downtime. In contrast, the starter cost of the channel manufacturing equipment used in this report is approximately 300 USD; this is comparable to the least expensive way of producing a master mold, (such as using polydimethylsiloxane (PDMS)-based techniques, but has the advantage that changes in channel design and the printing of new channels take significantly less time while maintaining surface roughness comparable to the leading manufacturing techniques for 200 µm wide channels5. We are able to cut a microfluidic chip in less than 5 minutes and for less than 1 USD.
In this protocol, data is recorded at a fixed capture point downstream from the tracer inlet through brightfield imaging using a D-SLR camera mounted with a macro lens. While the protocol was developed using a solution of fluorescein sodium salt in deionized water (DI), this imaging method is applicable to other types of dye, such as food coloring, as long as there is a linear relation between the tracer's intensity and concentration. The potential range of chemicals to use can be further expanded by considering their absorption spectrum and background lighting. However, we note that some food dyes are derived from plant materials and may contain more than one chemical species; caution should be employed when selecting the food coloring to be used to avoid conflicting outcomes.
The validity of this setup and protocol was verified by computing the experimental dispersion factor, f, for varying channel aspect ratio and experimental flow rate, and comparing it to its theoretical values for microchannels of rectangular cross-sections, as shown in Figure 7. We also computed the diffusion coefficient, κ, for single-species passive tracers under these varying experimental conditions. Table 1 reports the molecular diffusion coefficient of fluorescein sodium salt obtained from this experimental investigation. Specifically, the tabulated κ-values were computed from equation (3) by using experimental fits for the enhanced dispersion coefficient, K, and theoretical values for the dispersion factor, f. We report average values for four experiments on microchannels with varying aspect ratios (λ = 0.1, 0.25, and 0.5) and flow rates (0.05, 0.1, and 0.2 cm/s). For each, we also include the relative error with respect to the theoretical value10,11, κ = 5.70 x 10-6 cm2/s, demonstrating the accuracy of our method. Finally, for each set of experimental parameters we report the Péclet number and the nondimensional time range defined by dividing the dimensional time t when the experimental intensity curve deviates from the baseline, by diffusion time td = h2/(4κ). We include the nondimensionalized experimental time range to demonstrate that our system has entered the Taylor dispersion regime and therefore can be well-approximated by a Gaussian profile15. In fact, the observation times reported in the last two columns of Table 1, are approximately 2–5 (or more) times the diffusion time td.
Next, we extended the protocol to investigate multispecies ion interaction and separation. We report below our results from applying the Taylor dispersion experiment to a multispecies electrolyte solution made by mixing fluorescein sodium salt and blue food coloring in DI water. Figure 8 shows the time evolution of the inverted blue channel intensity curves at the camera capture point for three solutes: blue food coloring solution in DI water (–), fluorescein sodium salt solution in DI water (...), and mixed blue food coloring and fluorescein sodium salt solution in DI water (----). Each curve is the average of five experimental trials with one standard deviation in each direction (shading). The curves show the experiments with blue food coloring alone (–) reaching a minimum first, compared to the timescale of the maximum for the fluorescein sodium salt experiments (...). This is consistent with the fact that fluorescein sodium salt has a molecular diffusion coefficient one order of magnitude smaller than that of blue 1, the dye ingredient for the blue food coloring used16. The mixed solution experiments (----) highlight this timescale difference and the consequent ion separation visible through a concavity change in the intensity profile; the curve dips below the baseline first before turning upward and peaking above the baseline. In Figure 9 we plot the same mixed solution inverted blue channel intensity curve (----) overlaid with a curve obtained by summing the individual contributions of the blue food coloring experiments and the fluorescein sodium salt experiments (+++). The difference between the two curves underlines the effect that the ion-ion interaction has on the mixed solution intensity curve. When simply adding the two individual solute contributions, the (+++) curve presents a deeper minimum driven by the strong below-baseline contribution of the blue dye solution (shown as – in Figure 8), before the concavity changes on a longer timescale compared to the mixed solution curve (----). Finally, the sum curve shows again a higher peak above the baseline compared to the mixed curve, due to the fluorescein sodium salt solution behavior (shown as ... in Figure 8). The softer peaking along with the timescale shortening is an indication of the interaction between the blue food coloring and fluorescein sodium salt ions.
The intensity profiles in Figure 6, Figure 8, and Figure 9 exhibit skewness; this may be due to a few differences between classic Taylor dispersion theory2,5,9 and the quantity measured in the experiments. The concentration profile predicted by equation (2) is symmetric in space, but in our experimental setup the measurement is taken at a fixed capture point downstream from the tracer injection site as a function of time. When viewed as a function of time, the resulting profile is inherently skewed. This temporal asymmetry is consistent with observations reported in previous studies, including Taylor and Harris (2019)5. Another possible cause of skewness is the influence of the finite area of the experimental image capture window. A possible alternative to the Gaussian fit described in equation (1), involves fitting the experimental data to the integral of the Gaussian expression in equation (2) over the finite image capture region (in x), as done in Bharadwaj, Santiago, and Mohammadi (2002)17. This contribution to skewness becomes particularly relevant when the size of the capture box is comparable to the standard deviation of the Gaussian curve; here, the length of our capture window is always at least one order of magnitude smaller than the Gaussian’s standard deviation.
This low-cost experimental method provides an accessible approach to the Taylor dispersion experiment at the microscale. The most delicate step in the protocol is the manufacturing and removal of the microchannel negative. During the manufacturing process, extra care must be taken to ensure the channel is secure before cutting to prevent miscuts. When removing the negative, ensure no material is left behind and avoid any contact with the channel sidewalls, which need to be smooth, parallel, and straight to ensure reliable experimental outcomes. A limitation of this method is the inherent xurography resolution limit. In this manuscript, the most difficult channels to produce are those with width w = 200 μm (and aspect ratio λ = 0.5), which pushed against the limit of the craft cutter resolution5. The primary cause of error is the stepper motor employed by the craft cutter, which moves the blades in defined step increments based on mechanical gears. When designs require cuts to be in between the defined step increment, greater error is introduced. In-depth work identifying the resolution limits of this xurography method is available in the literature5.
This experimental procedure provides a simple way to compute the enhanced dispersion factor, K, and molecular diffusion coefficient, κ, of single-species passive tracers. Additionally, the protocol offers a straightforward way of visualizing the interaction and separation dynamics between ion species. Given the accessibility and versatility of the platform, this method is suitable for analyzing the dynamics between ion species and further understanding the complex interplay of transport phenomena and it can be readily employed in applications such as a micromixer.
| | | | | Nondimensional time |
| Aspect ratio, λ | Flow rate (cm/s) | Experimental κ (cm2/s) | Relative error | Péclet number (Pe) | tmin/td | tmax/td |
| 0.1 | 0.02 | 5.813 x 10-6 ± 3.797 x 10-7 | 1.982 x 10-2 | ~ 18 | ~ 30 | ~ 52 |
| 0.25 | 0.05 | 5.333 x 10-6 ± 4.179 x 10-7 | 6.443 x 10-2 | ~ 44 | ~ 11 | ~ 27 |
| 0.25 | 0.1 | 5.655 x 10-6 ± 2.822 x 10-7 | 7.838 x 10-3 | ~ 88 | ~ 6 | ~ 16 |
| 0.25 | 0.2 | 5.978 x 10-6 ± 1.724 x 10-7 | 4.884 x 10-2 | ~ 175 | ~ 2 | ~ 10 |
| 0.5 | 0.1 | 5.444 x 10-6 ± 4.790 x 10-7 | 4.496 x 10-2 | ~ 88 | ~ 6 | ~ 16 |
Table 1: Experimental molecular diffusion coefficient (κ) for fluorescein sodium salt. Results are computed from equation (3) by using experimental fits for the enhanced dispersion coefficient, K, and theoretical values for the dispersion factor, f. Each row reports the average κ-value (and related standard deviation) for four experiments on microchannels with a specified aspect ratio (λ = 0.1, 0.25, or 0.5) and flow rate (0.05, 0.1, or 0.2 cm/s). For each, we include the relative error with respect to the theoretical value10,11, κ = 5.70 x 10-6 cm2/s, to demonstrate the accuracy of our method. Additionally, for each row we list the experimental Péclet number and the nondimensional time range defined by dividing the dimensional time t when the experimental intensity curve deviates from the baseline, by diffusion time td = h2/(4κ).

Figure 8: Time evolution of averaged inverted blue channel tracer intensity at the camera capture point for three tracers. Time evolution of averaged inverted blue channel tracer intensity at the camera capture point for three tracers: solution of blue food coloring in DI water (at concentration ratio food coloring:DI = 1:20 mL, –), solution of fluorescein sodium salt in DI water (at concentration 0.6 g/L, ...), and a mixed solution containing both blue food coloring and fluorescein sodium salt with the same concentrations as in their individual tracer experiments (----), i.e. blue food coloring:DI = 1:20 mL and 0.6 g/L of fluorescein. Each curve is the average of five experimental trials with one standard deviation in each direction (shading). Please click here to view a larger version of this figure.

Figure 9: Time evolution of averaged inverted blue channel tracer intensity at the camera capture point for mixed solution. Time evolution of averaged inverted blue channel tracer intensity at camera capture point for mixed solution containing blue food coloring and fluorescein sodium salt (----) with blue food coloring:DI = 1:20 mL and 0.6 g/L of fluorescein, and a sum curve (+++) combining the intensity of the blue food coloring solution experiments (solid curve in Figure 8, –) and fluorescein sodium salt solution experiments (dotted curve in Figure 8, ...). The mixed curve is the average of five experimental trials with one standard deviation in each direction (shading). The standard deviation of the sum curve is calculated by taking the square root of the sum of the standard deviations squared from the experiments with each individual tracer solution. Please click here to view a larger version of this figure.