Microfluidic systems can deliver portable point-of-care diagnostics without the need for external equipment or specialist operators, by integrating all reagents and manipulations required for a particular assay in one device1. A key approach is to deposit picogram quantities of dried reagents in microchannels with micrometre precision using specialized inkjet plotters2,3,4,5. This means that reagents can be stored for long periods of time and reconstituted spontaneously when adding a liquid sample. But it is challenging to carry out complex operations using multiple reagents, because shear flow enhances their dispersion and they tend to accumulate at moving liquid fronts, resulting in poor spatiotemporal control over the concentration profile of the reconstituted reagents6. One solution is to limit the rate of release of reagents into the liquid7,8,9,10. However, this requires the fine-tuning of different reagents, conditions and targeted operations, and cannot readily produce the complex, time-dependent multireagent concentration pulses required for sophisticated on-chip assays. Here we report and characterize a capillary flow phenomenon that we term self-coalescence, which is seen when a confined liquid with a stretched air–liquid interface is forced to ‘zip’ back onto itself in a microfluidic channel, thereby allowing reagent reconstitution with minimal dispersion. We provide a comprehensive framework that captures the physical underpinning of this effect. We also fabricate scalable, compact and passive microfluidic structures—‘self-coalescence modules’, or SCMs—that exploit and control this phenomenon in order to dissolve dried reagent deposits in aqueous solutions with precise spatiotemporal control. We show that SCMs can reconstitute multiple reagents so that they either undergo local reactions or are sequentially delivered in a flow of liquid. SCMs are easily fabricated in different materials, readily configured to enable different reagent manipulations, and readily combined with other microfluidic technologies, so should prove useful for assays, diagnostics, high-throughput screening and other technologies requiring efficient preparation and manipulation of small volumes of complex solutions.
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The data that support the findings of this study are available from the corresponding authors on request.
The code for the Schwarz–Christoffel mapping of self-coalescence (using Matlab), as well as the code for reagent pulse shaping (using Maple), is available on request from T.G.
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O.G., Y.T. and E.D. thank W. Riess for continuous support, and acknowledge partial funding from the European Union’s 7th Framework programme Chips4Life project (278720) and the IBM Research Frontiers Institute. O.G. and E.D. thank Coris BioConcept for discussions on DNA-amplification technologies, and microfluidic ChipShop for the fabrication of polymer prototypes using injection moulding. T.G. thanks C. Boudoux and S. Prudhomme (from the École Polytechnique de Montréal) for useful discussions. T.G. acknowledges support from the Natural Sciences and Engineering Council of Canada (NSERC; RGPIN2014-06409), the Fonds de Recherche du Québec–Nature et Technologies (FRQNT), and CMC microsystems.
The authors declare no competing interests.
Publisher’s note Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.
Peer review information Nature thanks Piotr Garstecki and the other, anonymous, reviewer(s) for their contribution to the peer review of this work.
Extended data figures and tables
a, Bright-field microscope images of microfluidic chips in silicon, each chip being composed of a rounded inlet (left), an SCM (middle), and a meandering channel (right) used for conveniently measuring the concentration profile of the solution exiting the SCM. b, Amaranth solutions from an SCM (left) and in a control microchannel (right) are readily visualized using the meandering channels. c, Calibration curve for quantification of the concentration of reconstituted amaranth (n = 4 for each concentration). Error bars represent standard error of the mean. d, Concentration profiles of amaranth solution reconstituted in SCMs or control microchannels (Qin = 500 nl min−1). Means of individual acquisitions are displayed with dark coloured lines and individual acquisitions with a lighter shading. Amaranth solution was inkjet spotted into SCMs at 100 ng mm−1 (250-µm pitch). The reagent accumulation in the control was so strong that the amaranth solution was diluted ×30 before deposition to keep the absorbance signal in the dynamic range of the camera. The concentration profile from control experiments shown in Fig. 2d is scaled up from this diluted signal.
Extended Data Fig. 2 Fabrication steps for SCMs with depressed barriers, and scanning electron microscopy images of representative SCMs.
a, Silicon wafers are processed by standard photolithography and multiple steps of deep reactive-ion etching (DRIE). Specifically, a 1.2-µm-thick AZ 6612 photoresist layer is patterned (step 1) to mask the SiO2 layer during etching in buffered hydrofluoric acid (BHF; step 2). A new layer of AZ 6621 is patterned (step 3), exposing the areas that are etched to form the trenches during the first DRIE step (step 4). Later, using the patterned SiO2 layer as the mask, a second DRIE step forms the microchannels while preserving the trenches (step 5). After dicing, the chips are cleaned and silanized in trichloro(octyl)silane solution (step 6). After reagent deposition, chips are sealed with a layer of polydimethylsiloxane (PDMS; step 7). b, Image of an SCM fabricated in silicon, with yellow frames highlighting particular regions shown below. c, The leading barrier with a trench geometry. Here, for visual clarity, the trench width is 20 µm, but 5-µm-wide trenches were used in experiments. The curved end of the leading barrier facilitates the initiation of self-coalescing flow. d, Diversion barrier with a step-down geometry. e, Raised vertical CPLs at the entrance of the SCM help to keep the meniscus away from the side wall coloured in blue. f, The barrier at the vent entrance (arrowhead) ensures that liquid does not enter the vent. The depths of the SCM (HSCM), outlet (Houtlet) and barriers (Hbarrier) are shown on the images. g, h, Scanning electron microscopy (SEM) images of the devices used in G6PDH reactions (g) and in RPA reactions (h). (The numbers 1-2 and 1-4 are device numbers.).
a, Bright-field microscope images of devices fabricated in silicon (numbered 1-1 to 1-5) in which volume scaling experiments were performed. As discussed in Fig. 1d, the velocity of the self-coalescing flow decays more quickly in narrower than in wider SCMs. In order to maintain a quick decay of the self-coalescing flow velocity in wide SCMs, the leading barrier is simply shifted towards the area in which reagents are deposited. Amaranth is deposited at 100 ng mm−1 (250-µm pitch). A spotting alignment mark is used to align the inkjet spotter head with the microfluidic chips for precise targeting of the deposition location. b, Bright-field microscope images showing the amaranth solution in the meandering channels, reconstituted in the SCMs shown in panel a. c, Time series of bright-field microscope images showing the reconstitution of amaranth in a 1-mm-wide SCM (Qin = 500 nl min−1). Typically, in wide SCMs (wider than 0.5 mm), lateral homogenization of the reconstituted reagent is complete at the narrow outlet of the SCM (as seen here), and can be enhanced, if necessary, by adding a Dean vortex mixer, a chaotic mixer, or a simple meandering channel. Larger volumes of solution with reconstituted reagents can also be achieved using an array of parallel SCMs. SCMs are easily scaled; however, making them longer decreases the maximum filling flow rate because the pressure at the inlet needs to be lower than the Laplace pressure over the CPL.
a, During longitudinal flow, the hydraulic pressure (Phydraulic) increases as the hydraulic resistance (Rhydraulic) increases with the distance travelled by the liquid. The leading barrier is able to preserve the longitudinal flow as long as the pinning forces (PLaplace) can balance the increasing hydraulic pressure and the pressure exerted by the resistance to wetting (Rwetting). In order to investigate this effect, the width (W = 75, 100, 125, 150, 175 or 200 µm) and the height (H = 30, 45 or 90 µm) of the longitudinal flow area and the filling flow rate (Qin = 0.75, 1.5 or 3.0 µl min−1) were varied. During experiments, the maximum distance along which the liquid remains pinned was measured. b, Bright-field (left) and SEM (right) images of devices in which stability-assessment experiments are performed. c, Experimental data support theoretical predictions that: first, a smaller liquid–vapour interface can bear a higher hydraulic pressure; second, the hydraulic radius of the longitudinal flow area needs to be large in order to fill deeper structures or for high filling flow rates; and third, the flow rate challenges the stability of the leading barrier. Data points are means of experiments (n = 8 or more; error bars represent standard error of the mean). Conditions in which the liquid was not pinned at the CPL (longitudinal flow length = 0 mm) or the liquid travelled to the end of the test device (longitudinal flow length = 65 mm) are excluded from the plot.
a, Illustration of the experimental method for analysing dispersion in SCMs and in downstream channels at distance d. C, concentration. b–g, Predicted concentration profiles for experiments shown in Fig. 4 (C(t) in arbitrary units). b, c, Results of controlling the spotting pitch to generate spiked (b) or flat (c) concentration pulses at optimal (Pé = 5.6; top panels) and large (Pé = 100; lower panels) Péclet numbers, at constant spotted reagent mass. d, Signal decorrelation over time due to Taylor–Aris dispersion for several positions of the detection zone (Pé = 13). e, Pulsing of two spatially resolved different reagents (Pé = 13). f, Pulsing of a flat profile of two mixed reagents by alternated spotting and flow control (Pé = 13). g, Pulsing of two linear concentration gradients to a detection zone (Pé = 13).
A chamber of volume Vdelay at the entrance of the vent adds a delay before a liquid leaves the SCM. a, Time series of images showing filling of the delay chamber while reconstituted amaranth diffuses. Reagents in area A, but not in area B, have additional time to reconstitute/diffuse while the rest of the SCM fills (t = 0 s). If needed, using a delay chamber gives additional time for the reconstitution/diffusion of the B reagents. Arrowheads mark the liquid filling front in the delay chamber. b, Effect of delay on the concentration profile of points A and B. Without any delay, point B disperses more than it does with a delay, and its profile is broader (n = 9; Qin = 200 nl min−1). c, Measured delay provided by different delay chambers. The dashed line is the identity line; error bars represent standard error of the mean; n = 6; Qin = 200 nl min−1.
a, b, Optimization data for SYBR Green concentration (a; four experiments) and Mg2+ concentration (b; five experiments) for amplification of ten copies per microlitre of HPV-18 DNA. c, DNA concentration calibration (seven experiments) for HPV-18 DNA quantification. Plots show amplification onset time extracted from SYBR Green fluorescence signals. Error bars represent standard errors of the mean.
a, Bright-field image of the device in which reagent pulse shaping and complex profile generation experiments were performed. The diversion barrier of these SCMs has a trench geometry in order to keep the dimensions of the dispersion analysis channel identical to the dimensions of the SCM. b, Absorbance calibration curve, and, c, the calibration curve after linear spectral unmixing of the amaranth signal. d, e, As for panels b, c, but for the brilliant blue signal. n = 6 for each data point. Error bars represent standard errors of the mean.
a, The setup for filling SCMs and documenting the dissolution of food dyes. b, Filling SCMs manually using a micropipette for G6PDH quantification experiments. c, Measuring the fluorescence signal from G6PDH and RPA reactions using a microtitre plate reader fitted with a custom-made aluminium adaptor.
This file contains additional information and equations on the theoretical framework.
4.8 µm fluorescent microspheres suspended in a liquid are injected into an SCM (0.5-mm-wide) at 0.5 µl min−1 flow rate. The video is in real time with each frame acquired over a 60 ms exposure.
An SCM (L×W×D, 5 mm × 0.5 mm × 50 µm) spotted with amaranth dye is filled with water at 0.5 µl min−1 flow rate. The video is accelerated (3×).
Filling of an SCM observed using fluorescent microparticles. The experimental image is only the top half of the video. The part below the central mirror symmetry line (located at the device wall) is simply a reflection of the upper half made to highlight a similitude between self-coalescence and Saffman–Taylor viscous fingering. The height of the SCM is 50 µm and its width is 500 µm with a flow rate of 0.5 µL min−1 and λ = 1/2. The video is shown along with the discussion in Supplementary Information, section 1.5.2
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Gökçe, O., Castonguay, S., Temiz, Y. et al. Self-coalescing flows in microfluidics for pulse-shaped delivery of reagents. Nature 574, 228–232 (2019). https://doi.org/10.1038/s41586-019-1635-z
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