The present invention relates to, inter alia, systems and methods for measuring contact-line mobility of inertially spreading liquids.
Contact-line mobility characterizes how fast a liquid can coat or uncoat a substrate support. During rapid movement of liquid across a supporting substrate, contact angles and contact line speeds change dynamically. Mobility captures this far-from-equilibrium behavior. For sufficiently rapid movement, the flow is largely inviscid and surface tension and liquid inertia compete to influence the interface shape near the support.
While standard goniometry techniques address the issue of determining the static contact angle and the contact angle hysteresis of a substrate-liquid-gas system, there is no current standard for measuring the mobility of the contact line in terms of the velocity dependence of the contact angle.
There is a need for new and improved technologies for measuring contact-line mobility of inertially spreading liquids.
The present invention is directed to overcoming these and other deficiencies in the art.
The present disclosure relates to, inter alia, systems and methods for measuring contact-line mobility of a liquid on a solid substrate.
In one aspect, the present disclosure provides a system for measuring contact-line mobility of a liquid on a solid substrate, where the system includes: (a) a motion-generation component; (b) a motion-measurement component; and (c) a computer component. The motion-generation component of the present system includes an actuator and a controller, where (i) the actuator is adapted to mount a solid substrate, and effective to impart periodic forcing to the solid substrate when a test droplet of the liquid is deposited thereon; and (ii) the controller is adapted to tune frequency and amplitude of the forcing to induce measurable contact-line displacement of the test droplet on the solid substrate. The motion-measurement component of the present system includes an image acquisition device adapted for capturing images of the test droplet deposited on the solid substrate before, during and/or after the forcing imparted by the actuator. Furthermore, the image acquisition device has requisite spatial and temporal resolution to enable acquisition of image data of the test droplet, where the image data includes contact-line displacement, contact-line speed, and contact angle at or near contact-line. The computer component of the present system is adapted to receive and analyze the image data from the motion-measurement component effective to measure the contact-line mobility of the test droplet.
In another aspect, the present disclosure provides a method for measuring contact-line mobility of a liquid on a solid substrate. The method includes the steps of: (a) subjecting test droplets of the liquid on the solid substrate to periodic forcing to induce measurable contact-line displacement; (b) acquiring image data of the test droplets comprising contact-line displacement, contact-line speed, and contact angle at or near contact-line thereof; and (c) determining Contact-Line Drag Coefficient M from the image data by generating a contact-line cyclic diagram. The contact-line cyclic diagram includes a plot of ηΔα versus η{dot over (η)}, where η=contact line displacement, {dot over (η)}=contact-line speed, and Δα=contact angle deviation. The contact-line cyclic diagram include also includes an advancing loop A having a linear region A and a receding loop R having a linear region R simultaneously, where the Contact-Line Drag Coefficient M is a reciprocal slope of a best fit line through linear region A and linear region R.
In another aspect, the present disclosure provides a further method for measuring contact-line mobility of a liquid on a solid substrate. This method includes the steps of: (a) providing a system for measuring contact-line mobility of a liquid on a solid substrate, where the system includes a motion-generation component, a motion-measurement component, and a computer component adapted to receive and analyze the image data from the motion-measurement component; (b) depositing one or more test droplet of the liquid onto the solid substrate; and (c) operating the system in a manner effective to determine the Contact-Line Drag Coefficient M of the liquid. The motion-generation component of the system includes an actuator and a controller. The actuator is adapted to mount a solid substrate thereon, and effective to impart periodic forcing to the solid substrate when a test droplet of the liquid is deposited thereon. The controller is adapted to tune frequency and amplitude of the forcing to induce measurable contact-line displacement of the test droplet on the solid substrate. The motion-measurement component includes an image acquisition device adapted for capturing images of the test droplet deposited on the solid substrate before, during, and/or after the forcing imparted by the actuator. The image acquisition device has requisite spatial and temporal resolution to enable acquisition of image data of the test droplet comprising contact-line displacement, contact-line speed, and contact angle at or near contact-line. The computer component is configured to determine a dimensionless parameter of contact-line mobility of the liquid from the image data, where the dimensionless contact-line mobility parameter is Contact-Line Drag Coefficient M.
Some advantages of the system and methods of the present disclosure include, for example, those described below. For example, the system and methods of the present disclosure implement key innovations involving combining contact-line (CL) displacement, CL speed, and contact angle (CA) data in a way to reveal linearity (see
Wing regions data represent behavior far from stick-slip region. This is dynamical behavior, far from equilibrium. One major innovative contribution of the present disclosure is revealing how to characterize this far-from-equilibrium behavior (see
The present disclosure provides various advantages, including, without limitation: (i) identifying that there exists a linear region in a contact-line cyclic diagram for CL mobility; (ii) showing how to combine measurements of CL displacement, CL speed, and CA to reveal that linear region; (iii) showing that there are limits to that region of linearity (the wing regions), that are not obvious in the traditional diagram (TD) (see
Incidentally, the systems and methods of the present disclosure enable a broad set of industrial applications, as disclosed herein.
These and other objects, features, and advantages of this invention will become apparent from the following detailed description of the various aspects of the invention taken in conjunction with the accompanying drawings.
For the purpose of illustrating aspects of the present invention, there are depicted in the drawings certain embodiments of the invention. However, the invention is not limited to the precise arrangements and instrumentalities of the embodiments depicted in the drawings. Further, if provided, like reference numerals contained in the drawings are meant to identify similar or identical elements.
The present invention relates to, inter alia, systems and methods for measuring contact-line mobility of inertially spreading liquids. The systems and methods can be used in various ways, including, without limitation, for material characterization for application in forensic examination of blood splats, inkjet printing, additive manufacturing, and immersion lithography, just to name some.
Resonantly-Driven Droplets (RDD) allow measurement of an important property of rapidly moving contact-lines-the mobility. The mobility is a measure of how fast the contact line moves per deviation of the contact-angle from the equilibrium contact-angle. It is a dynamical characterization of how liquids move across supporting substrates. In RDD, the bulk resonance of the drop amplifies the small and fast CL motion sufficiently to be measurable. The RDD approach enables measurement of a CL mobility and to infer a CL dissipation for droplets on hydrophobic and hydrophilic surfaces, surfaces with varying contact-angle hysteresis. Rapid spreading is important in many industrial, manufacturing and natural settings. Mobility is a non-equilibrium characterization that complements conventional static contact angle and contact angle hysteresis measurements (advancing and receding contact angles). The present disclosure is directed to aspects relating to RDD.
The systems and methods of the present disclosure provide various advantages over the state of the art relating to mobility measurements of liquids. Examples of just some of the advantages include, without limitation, the following: (i) speed (e.g., time required for data collection is on the order of a tenth of a second; (ii) reproducibility (e.g., periodic nature of setup allows repeat measurements to be taken in rapid succession); and (iii) robustness (e.g., results insensitive to details of the operating parameters).
In one aspect, the present disclosure provides a system for measuring contact-line mobility of a liquid on a solid substrate, where the system includes: (a) a motion-generation component; (b) a motion-measurement component; and (c) a computer component. An illustrative example of one embodiment of the system of the present disclosure is schematically shown in
The motion-generation component of the present system includes an actuator and a controller, where (i) the actuator is adapted to mount a solid substrate, and effective to impart periodic forcing to the solid substrate when a test droplet of the liquid is deposited thereon; and (ii) the controller is adapted to tune frequency and amplitude of the forcing to induce measurable contact-line displacement of the test droplet on the solid substrate.
The motion-measurement component of the present system includes an image acquisition device adapted for capturing images of the test droplet deposited on the solid substrate before, during and/or after the forcing imparted by the actuator. Furthermore, the image acquisition device has requisite spatial and temporal resolution to enable acquisition of image data of the test droplet.
As used herein, the term “image data” of the test droplet includes contact-line displacement, contact-line speed, and contact angle at or near contact-line.
The computer component of the present system is adapted to receive and analyze the image data from the motion-measurement component effective to measure the contact-line mobility of the test droplet.
In one embodiment of the system, the computer component is configured to determine a dimensionless parameter of contact-line mobility of the liquid from the image data. The dimensionless contact-line mobility parameter is referred to herein as the Contact-Line Drag Coefficient M.
As used herein, the “Contact-Line Drag Coefficient M” is determined from the image data by generating a contact-line cyclic diagram that includes a plot of ηΔα versus η{dot over (η)}, where η=contact line displacement, {dot over (η)}=contact-line speed, and Δα=contact angle deviation. The contact-line cyclic diagram includes an advancing loop A having a linear region A and a receding loop R having a linear region R simultaneously, where the Contact-Line Drag Coefficient M is a reciprocal slope of a best fit line through linear region A and linear region R. In certain embodiments, the contact-line cyclic diagram is generated using a contact angle balancing computation that involves minimizing angle φ over reference contact angle
In one embodiment of the system of the present disclosure, the motion-generation component is configured to create inertial-capillary motions in bulk accompanied by contact-line motion sufficient to enable contact-line displacement, contact-line speed, and contact angle at or near contact-line to be measured by the motion-measurement component, with requisite spatial and temporal resolution. In a particular embodiment, the contact-line motion is periodic motion.
In one embodiment of the system of the present disclosure, the motion-generation component is configured to induce periodic forcing of the test droplets by substantially plane-normal motion of the solid substrate.
In one embodiment, the actuator is a mechanical shaker device.
In one embodiment, the controller is a function generator for controlling plane-normal vibration parameters of the actuator.
In one embodiment of the system of the present disclosure, the image acquisition device is adapted for capturing different views of the images of the test droplet. The different views of the images can include one or more top view, bottom view, side view, or combination of top views, bottom views, or side views. As used herein, a side view encompasses all angles of views of the test droplet that are not the top or bottom view thereof.
In one embodiment, the image acquisition device is a high-speed camera.
In one embodiment, the image acquisition device is effective to capture high-speed images of the test droplet at frame rates including, but not limited to, a range of about 2000-5000 Hz, including any frame rates in between this range.
In other embodiments, the system of the present disclosure can further include a liquid dispensing component configured to dispense one or more test droplets onto the solid substrate during functioning of the system. The liquid dispensing component can include, without limitation, any device or system that can dispense the liquid test droplets in any manner and volume effective for the intended operation of the systems and methods of the present disclosure including, for example, devices and systems that operate in a manual, automated, robotic, computerized, or other suitable fashion. One suitable example of a liquid dispensing component can include, without limitation, a microsyringe, including a manually or automatically operated microsyringe or a plurality of microsyringes.
As used herein, the “solid substrate” can include any solid material that is a solid substrate. As used as a part of a system of the present disclosure or in a method of the present disclosure, a solid substrate can be any solid material in any form and in any orientation suitable to enable measurement of a liquid's contact-line displacement, contact-line speed, and contact angle at or near contact-line by an image acquisition device of the present disclosure with the requisite spatial and temporal resolution as described herein. Without intending to be limited thereby, provided below are suitable examples of various solid substrates of the present disclosure. In one embodiment, the solid substrate is a substantially planar solid substrate. In one embodiment, the solid substrate can be horizontally oriented, vertically oriented, or oriented in any other plane between the horizontal and vertical orientations. In one embodiment, the solid substrate can be in the form of a platform, including, without limitation, a platform mounted on the motion-generation component of the present disclosure or more specifically mounted on the actuator of the motion-generation component. In one embodiment, the solid substrate can include, without limitation, a smooth and hydrophobic material. In one embodiment, the solid substrate can include, without limitation, silicon, glass, mica, or metal. In one embodiment, the solid substrate is in the form of a silicon wafer, a glass wafer, or a freshly cleaved mica. In one embodiment, the solid substrate is in the form of a polished and hydrophobic silicon or glass wafer, or similarly prepared metal. In one embodiment, the surface of the solid substrate is treated to have a low-hysteresis (LH) surface. In one embodiment, the surface of the solid substrate is either hydrophobic, hydrophilic, or a combination thereof. In one embodiment, the coating/uncoating of the solid substrate can occur, without limitation, on a gel or other material.
In another aspect, the present disclosure provides a method for measuring contact-line mobility of a liquid on a solid substrate. The method includes the steps of: (a) subjecting test droplets of the liquid on the solid substrate to periodic forcing to induce measurable contact-line displacement; (b) acquiring image data of the test droplets comprising contact-line displacement, contact-line speed, and contact angle at or near contact-line thereof; and (c) determining Contact-Line Drag Coefficient M from the image data by generating a contact-line cyclic diagram. The contact-line cyclic diagram includes a plot of ηΔα versus η{dot over (η)}, where η=contact line displacement, {dot over (η)}=contact-line speed, and Δα=contact angle deviation. The contact-line cyclic diagram include also includes an advancing loop A having a linear region A and a receding loop R having a linear region R simultaneously, where the Contact-Line Drag Coefficient M is a reciprocal slope of a best fit line through linear region A and linear region R.
Although specific embodiments of the method are described below, the systems described herein and the components of those systems can all be used to implement the methods of the present disclosure described in more detail below. Therefore, the disclosures of certain embodiments of the method described below are not meant to be limiting on the systems and components that can be used to perform the method.
In one embodiment of this method, the contact-line cyclic diagram is generated using a contact angle balancing computation comprising minimizing angle φ over reference contact angle
In one embodiment of this method, the subjecting step (a) involves subjecting the test droplets on the solid substrate to inertial-capillary motions in bulk, and accompanied by contact-line motion, under conditions sufficient to enable contact-line displacement, contact-line speed, and contact angle at or near contact-line to be measured by an image acquisition device with requisite spatial and temporal resolution.
The method is suitable for measuring contact-line mobility of any liquid, including, without limitation, a liquid such as a blood sample, an ink sample, a drop-on-demand printing liquid sample, a 3D printing liquid sample, an additive doped liquid sample, an immersion lithography liquid sample, a spin-coating liquid sample, a soldering liquid sample, a brazing liquid sample, and a lubricant liquid sample.
In another aspect, the present disclosure provides a further method for measuring contact-line mobility of a liquid on a solid substrate. This method includes the steps of: (a) providing a system for measuring contact-line mobility of a liquid on a solid substrate of the present disclosure; (b) depositing one or more test droplet of the liquid onto the solid substrate; and (c) operating the system in a manner effective to determine the Contact-Line Drag Coefficient M of the liquid.
In accordance with this method, the system used in this method includes the system described in the present disclosure. In particular, the system used in this method includes a motion-generation component, a motion-measurement component, and a computer component adapted to receive and analyze the image data from the motion-measurement component.
The motion-generation component of the system includes an actuator and a controller. The actuator is adapted to mount a solid substrate thereon, and effective to impart periodic forcing to the solid substrate when a test droplet of the liquid is deposited thereon. The controller is adapted to tune frequency and amplitude of the forcing to induce measurable contact-line displacement of the test droplet on the solid substrate.
The motion-measurement component includes an image acquisition device adapted for capturing images of the test droplet deposited on the solid substrate before, during, and/or after the forcing imparted by the actuator. The image acquisition device has requisite spatial and temporal resolution to enable acquisition of image data of the test droplet comprising contact-line displacement, contact-line speed, and contact angle at or near contact-line.
The computer component is configured to determine a dimensionless parameter of contact-line mobility of the liquid from the image data, where the dimensionless contact-line mobility parameter is Contact-Line Drag Coefficient M.
In accordance with this method, in one embodiment, the Contact-Line Drag Coefficient M is determined from the image data by generating a contact-line cyclic diagram that includes a plot of ηΔα versus η{dot over (η)}, wherein η=contact line displacement, {dot over (η)}=contact-line speed, and Δα=contact angle deviation. The contact-line cyclic diagram includes an advancing loop A having a linear region A and a receding loop R having a linear region R simultaneously, where the Contact-Line Drag Coefficient M is a reciprocal slope of a best fit line through linear region A and linear region R.
In accordance with this method, in one embodiment, the contact-line cyclic diagram is generated using a contact angle balancing computation that involves minimizing angle φ over reference contact angle
In accordance with this method, in one embodiment, the motion-generation component is configured to create inertial-capillary motions in bulk accompanied by contact-line motion sufficient to enable contact-line displacement, contact-line speed, and contact angle at or near contact-line to be measured by the motion-measurement component, with requisite spatial and temporal resolution.
In one embodiment, the contact-line motion is periodic motion.
In accordance with this method, in one embodiment, the motion-generation component is configured to induce periodic forcing of the test droplets by substantially plane-normal motion of the solid substrate.
In one embodiment, the actuator includes, without limitation, a mechanical shaker device.
In one embodiment, the controller includes, without limitation, a function generator for controlling plane-normal vibration parameters of the actuator.
In accordance with this method, in one embodiment, the image acquisition device is adapted for capturing different views of the images of the test droplet. The different views of the images can include one or more top view, bottom view, side view, or combination of top views, bottom views, or side views. As used herein, a side view encompasses all angles of views of the test droplet that are not the top or bottom view thereof.
In one embodiment of this method, the image acquisition device is a high-speed camera.
In other embodiments of this method, the one or more test droplet is dispensed onto the solid substrate by a liquid dispensing component of the system. Suitable examples of liquid dispensing component can include, without limitation, a manual microsyringe. However, the method can involve any other liquid dispensing component as described herein.
This method is suitable for measuring contact-line mobility of any liquid, including, without limitation, a liquid such as a blood sample, an ink sample, a drop-on-demand printing liquid sample, a 3D printing liquid sample, an additive doped liquid sample, an immersion lithography liquid sample, a spin-coating liquid sample, a soldering liquid sample, a brazing liquid sample, and a lubricant liquid sample.
In accordance with the methods of the present disclosure, in one embodiment, the resonant frequency of the test droplet is determined by analyzing high-speed side-view profile images of the test droplet while a shaker device is signaled by the function generator to drive the test droplet in a plane-normal direction through mechanical vibrations.
In certain embodiments, the test droplet volume can be, without limitation, as large as possible (so as to reduce errors, if any, with optical measurements) without the droplet flattening into a puddle (which will inevitably happen with large enough volumes due to gravity).
In accordance with the systems and methods of the present disclosure, the hardware used for the system can include, without limitation, a mechanical shaker capable of receiving an input signal from a function generator as well as a high-speed image acquisition device. In certain embodiments, to make a measurement, the solid substrate in question is securely attached to the shaker with a small (under capillary length scale) drop of the liquid of interest deposited on the substrate. The shaker is made to undergo a frequency sweep to select the resonant frequency of the drop, at which the data acquisition will commence for several periods of oscillation at that constant frequency. With the image data collected, basic image analysis allows the evaluation of the contact line mobility parameter.
During the use of the systems and methods of the present disclosure, it is recognized that in certain instances mobility can be affected by the solid substrate as well as the liquid that is being coated or uncoated. For example, changing the solid substrate chemically or mechanically (e.g., roughening) or by some other means can change mobility.
These and other objects, features, and advantages of this invention will become apparent from the following detailed description of the various aspects of the invention taken in conjunction with the accompanying drawings.
Provided below is further disclosure with regard to the background, detailed description, and various embodiments and examples relating to the present invention.
The following examples are intended to illustrate particular embodiments of the present invention, but are by no means intended to limit the scope of the present invention.
Contact-line mobility characterizes how fast a liquid can wet or unwet a solid support by relating the contact angle Δα to the contact-line speed UCL. The contact angle changes dynamically with contact-line speeds during rapid movement of liquid across a solid. Speeds beyond the region of stick-slip are the focus of this experimental paper. For these speeds, liquid inertia and surface tension compete while damping is weak. The mobility parameter M is defined empirically as the proportionality, when it exists, between Δα and UCL, MΔα=UCL. We discover that M exists and measure it. The experimental approach is to drive the contact line of a sessile drop by a plane-normal oscillation of the drop's support. Contact angles, displacements and speeds of the contact line are measured. To unmask the mobility away from stick-slip, the diagram of Δα against UCL, the traditional diagram, is remapped to a new diagram by rescaling with displacement. This new diagram reveals a regime where Δα is proportional to UCL and the slope yields the mobility M. The experimental approach reported introduces the cyclically dynamic contact angle goniometer. The concept and method of the goniometer are illustrated with data mappings for water on a low-hysteresis non-wetting substrate.
The liquid/solid/gas contact line (CL) marks the boundary between wet and unwet support. A liquid advances along a support by displacing the surrounding gas. Alternatively, if the liquid retreats it may unwet the previously wet support, in which case gas replaces liquid. For CLs moving at high enough speeds, UCL, the contact-line motion is dominated by liquid inertia and capillarity. Rapidly advancing and retreating CL motions are relevant to a broad range of technological phenomena, from satellite propellant management (Srinivasan 2003) to harvesting energy through liquid metal CL motions (Krupenkin & Taylor 2011) to the immersion lithography approach to fabrication of semiconductor chips (Gnanappa et al. 2011).
In this example, we show experimentally that a single characterization of inertial spreading can be extracted from the cyclic measurements of rapid wetting and de-wetting. This lays the foundation for characterizing inertial-capillary spreading as a material-like parameter for liquid/solid/gas triplets. This possibility and the further work needed to realize this goal are discussed.
Practically speaking, a signature of inertial-capillary motions is underdamped vibrations. Water and liquid metal drops are important examples that exhibit underdamped motions. We choose water as liquid for our benchmark system. We use a slightly hydrophobic support with low hysteresis. In summary, inertial-capillary motion on a solid support is favoured by liquids that do not strongly wet that support and that have low bulk viscosity.
When disturbed from a reference configuration, the CL and contact angle (CA) will deviate by a displacement η and an angle Δα, respectively,
Our experimental set-up includes a droplet shaker and high-speed camera to image the contact-line region for subsequent analysis by computer,
Large CL excursions are favoured by low viscosity liquids on low-hysteresis coatings. Such liquids tend to have neutral affinity for the support; that is, a CA near 90°. Our benchmark system for this study is water on a silicon wafer treated with a silane coating to achieve a rest-state CA,
Relevant dimensional scales are given in Table 1. To stay below the capillary length scale, small droplets are used. The volume-based length D≡V1/3, where V is the drop volume, is approximately 2.7 mm for a drop volume of V=20 μL. This drop resonates at a measured frequency of approximately f=67 Hz, yielding a time scale 1/ω of approximately 2.4 ms, Table 1. In comparison, the typical capillary time scale τ≡(ρV/σ)1/2 is approximately 7 times longer. Alternative length scales include the typical plate excursion, A*, and the viscous layer thickness δ=(v/ω)1/2 which is approximately 0.05 mm. Note that this characteristic viscous layer is approximately half A* and approximately 1/50 the scale D. The comparison with D suggests that the viscous layer plays a limited role in the dynamics, at least for water. The observed CL velocity scale UCL is approximately 50% greater than the forcing velocity A*ω, attributed to the effectiveness of resonant excitation and to the low-hysteresis nature of the support coating. Finally, the typical acceleration is also approximately 50% greater than the acceleration of gravity. This suggests that significant deformation from the spherical cap shape may be expected.
TABLE 1. Scales: forcing, ω−1≡(2πf)−1; capillary, τ≡√{square root over (ρV/σ)}; volume-based length, D≡V1/3; typical forcing amplitude, A*; boundary layer thickness, δ≡√{square root over (v/ω)}; forcing speed, A*ω, CL speed, UCL; forcing acceleration A*ω2; maximum angle-deviation, Δα*; asterisk (*) denotes value fixed throughout the paper, a typical value used for scaling.
TABLE 2. Parameters, systems M00, F00: dimensional, drop of volume V driven at frequency f and acceleration a; dimensionless: definitions below symbols (subscripts: f=‘forcing’, o=‘observed’), volume-length D≡V1/3; note that UCL is a maximum; for system definitions, cf. Table 4.
TABLE 3. Water-glycerol mixture properties. Density and viscosity values based on empirical correlation (Cheng 2008). Surface tension values based on interpolation of experimental data (Glycerine Producers' Association 1963).
Dimensionless characterizations can be based on either the forced motion (subscript ‘f’) or the observed CL motion (subscript ‘o’), Table 2. Observed scales (e.g. UCL) often tend to better reflect the fluid dynamics but Table 1 for our experiments suggests little difference. Inertial-capillary spreading is characterized by Re>>1 and Cao<<1, as holds for M00. For both Weo and Cao characterizations, the local driving force for CL motion is the CA deviation, Δα, which is more accurately characterized as σ sin(Δαmax) rather than simply σ. For Δαmax˜10°, Table 1, the typical values listed in Table 2 are increased by nearly a factor of six. The Cao remains small but the revised Weo for M00 is much closer to one, consistent with the balance of inertia and capillarity in these motions.
There are many reviews of CL behaviour that include some combination of modelling, computation and measurement (Diez, Kondic & Bertozzi 2000; Pomeau 2001; Bonn et al. 2009; Savva & Kalliadasis 2011; Snoeijer & Andreotti 2013). Scarce mention of inertial-capillary CL motions is found in these. Snoeijer & Andreotti (2013) summarizes the situation where inertial-capillary behaviour is listed under future issues—‘new challenges for moving contact lines emerge from the . . . inclusion of liquid inertia’.
TABLE 4. System designation combines solid (M, F) and glycerol concentration (by volume) in water (xx %) where xx denotes 0, 20, 40, 50, 60%, Table 3, to yield M00, . . . , M60, and F00. CA measured using commercial goniometer, see Example 1, § 3.3.
Our literature review focuses on experimental work, justified by our example's focus on experiment. Inertial-capillary motion may be generated ‘naturally’ as in spreading by gravity (or capillarity) or be ‘forced’ as by a moving boundary. A traditional example of natural spreading occurs when gravity moves a drop down an inclined substrate (Mahadevan & Pomeau 1999; Aussillous & Quéré 2004; Hodges, Jensen & Rallison 2004). However, inertial motions may be the exception in such a set-up. Rapid natural transient motion driven by capillarity occurs in spreading on contact with a substrate (Bird, Mandre & Stone 2008; Carlson, Bellani & Amberg 2012; Winkels et al. 2012). Interest in these measurements has often been in the power law exponents characterizing the various spreading regimes. Sometimes, the relaxation of a contact line from an initial non-equilibrium configuration is aided by vibrational energy input (Andrieu, Sykes & Brochard 1994; Decker & Garoff 1996). Other kinds of forces used to drive transient inertial spreading include evaporation (e.g. Moffat, Sefiane & Shanahan 2009), impact (e.g. Yokoi et al. 2009), electromagnetic (e.g. Kocourek et al. 2006) and electrostatic (e.g. Sen & Kim 2009) forces.
Steady CL motions result from steady forcing motions. To achieve these, a set-up that plunges a tape into a liquid bath has been favoured by the coating flows community (Blake & Ruschak 1979). An advantage of this approach is that displacement (speed) rather than force (acceleration) is controlled and hence behaviour far from stick-slip can be readily achieved (Shen & Ruth 1998; Blake 2006; Kumar & Prabhu 2007). In their experiments, Perlin and co-authors (Ting & Perlin 1995; Jiang, Perlin & Schultz 2004; Perlin, Schultz & Liu 2004) drive a plunging plate in a cyclic manner. These studies report contact angle versus contact-line velocity diagrams that are more complicated than
Regarding the terminology ‘mobility’, some clarification is in order. Prior modelling and computational studies have introduced a function g(x), viewed as a single-valued representation of the CL behaviour, Δα=g(UCL) with 0=g(0) (cf.
Δα=ΛUCL or MΔα=UCL where M≡Λ−1, (1.1a,b)
with Λ=g′(0). Davis (1980) seems to have first introduced a Λ-like parameter, in his modelling of the moving CL of a meandering rivulet. Beginning with Hocking's use of this condition, it became known as the ‘Hocking condition’ even though Hocking attributed it to Davis (Hocking 1987). Borkar & Tsamopoulos (1991) refer to it as a ‘phenomenological parameter’, a ‘property’ of the materials involved, in their numerical study of liquid bridge oscillations. Lyubimov, Lyubimova & Shklyaev (2004, 2006) call Λ the ‘wetting parameter’ while Fayzrakhmanova & Straube (2009) use both terms, ‘Hocking condition’ and ‘wetting parameter’, in computational studies of vibrated inviscid drops. All these studies treat Λ as a way to model CL behaviour without complications of the observed multiplicity of contact angles for a given CL speed (hysteresis and associated nonlinearity).
We use the term ‘mobility’ in analogy with a particle subject to a force F that moves with a velocity U, MF=U. In Stokes flow M is called the ‘Stokes mobility’ and is just the inverse of the drag coefficient, M=U/F=1/(6πμR). In the CL case, the uncompensated Young-Dupré force acts around the perimeter (radius R) in a direction tangent to the substrate,
F=2πRσ[cos
If this is thought of as driving the CL motion, then UCL is given by, F=λUCL, where λ is the resistance or CL drag coefficient. In the case of small disturbances Δα and near-neutral wetting,
We begin by outlining the experimental procedure in Example 1, § 2 and detailing the materials and methods in Example 1, § 3. Section 4 of Example 1 follows with the basic experimental measurements presented in several different ways to highlight the distinctions between the regimes of motion. We propose in Example 1, § 5 the cyclic diagram which allows measurement of CL mobility, as detailed in Example 1, § 6. Section 7 of Example 1 discusses the robustness and generality of the proposed measurement procedure by looking at additional results. Finally, some concluding remarks are given in Example 1, § 8.
In this example, rapid contact-line motions are induced by forcing the drop near resonance. Prior studies (e.g. Whitehill, Neild & Stokes 2012) have driven drops in a similar fashion in order to observe spreading transients but do not study cyclic CL behaviour while other studies (e.g. Vukasinovic, Smith & Glezer 2007) have driven drops near resonance in order to achieve atomization but do not study CL behaviour.
Shapes of various modes that resonate at different frequencies are shown in
Trimethylsiloxy terminated poly(dimethylsiloxane) (PDMS) (Gelest, Product Code DMS-T22-100GM) was purchased from Gelest (Morrisville, Pa.). Silicon wafers (Silicon Quest International, catalogue no. 808-007) were purchased from Silicon Quest International (San Jose, Calif.). Sulphuric acid (95-98% min., MW 98.08, CAS #7664-93-9), toluene (99.5% min., MW 92.14, CAS #108-88-3) and acetone (CAS #67-64-1; Macron Chemicals) were purchased from VWM International (Radnor, Pa.). Hydrogen peroxide solution (50 wt. %, SKU 516813-500ML, CAS #7722-84-1, MW 34.01 g mol−1) was purchased from Sigma-Aldrich (St. Louis, Mo.). High-purity compressed nitrogen was purchased from Airgas (Radnor, Pa.). Glass vials (20 ml borosilicate glass scintillation vial, catalogue no. 03-337-5) and light mineral oil (CAS #8042-47-5) were purchased from Fisher Scientific (Pittsburgh, Pa.).
Relevant properties of the liquids used in this work are given in Table 3. Designations and key characterizations of solid-liquid systems are given in Table 4.
To prepare substrate M, a silicon chip with dimensions of approximately 2×1 cm is cleft from a silicon wafer and sonicated (Ultrasonic Cleaner, model B2500A-DTH, VWR) in water for 20 min to remove solid particles on the surface. Any organic contaminants are then removed by soaking the chip in piranha solution (70% sulphuric acid/30% hydrogen peroxide) for 20 min. The chip is rinsed in running de-ionized (DI) water (purified by an Elga Ultra SC MK2, Siemens) for 10 min, blow dried using high-purity compressed nitrogen and cleaned using oxygen plasma (Basic Plasma Cleaner, model PDC-32G, Harrick Plasma) at 600 μm for 1 min. The chip is placed in a freshly opened glass vial and wet with as-received PDMS. The vial is capped and baked at 100° C. for 24 h. After the vial cools to room temperature, the substrate is rinsed in turn with toluene, acetone and DI water.
Contact angle measurements are performed using an in-house MATLAB code and spot checked with a commercial goniometry software, DROPimage Advanced (Ramé-Hart Instrument Co., Succasunna, N.J.). An error analysis (Example 2, § 1) puts the uncertainty in the CA measurement code at ±1°.
A system consisting of a function generator (Agilent 33220A, Agilent Technologies, Santa Clara, Calif.), a power amplifier (Crown CE2000, Crown Audio, Elkhart, Ind.) and a mechanical vibrator (PASCO SF-9324, PASCO, Roseville, Calif.) similar to that used by Chang et al. (2013) is responsible for generating the mechanical vibrations. The solid sample surfaces are mounted horizontally on the vibrator. A manual microsyringe (Gilmont GS 1200, Cole-Parmer, Vernon Hills, Ill.) is used to dispense the test liquids. Typically, drops of 20 μl are used.
A RedLake HG-XL imaging system (DEL Imaging Systems, Cheshire, Conn.) fitted with a Tamron SP AF 90 mm f/2.8 Di Macro Lens (Tamron USA, Inc., Commack, N.Y.) is used to capture high-speed, side view images of the experiment. Typical frame rates used are in the range of 2000-5000 Hz. The typical spatial resolution is 10 μm pixel−1.
The useful measurements of the experiment are derived from the side view profile of the drop, supplemented by the measurement of support displacement. For instance, the contact-line velocity is approximated by the numerical time derivative of the drop profile where it joins the substrate. Meanwhile, the contact angle is measured using the tangent line of the drop profile at the contact line, as approximated using a secant method.
Where quantities are said to be scaled, the scaling factors are as follows (cf. Table 1). Length scale: A*=0.1 mm; time scale: σ*=17 ms; angular scale: Δα*=10°.
Where plots are given in red, blue and green colours, the colour coding denotes the following. Blue: |UCL|/max (UCL)>0.6, green: 0.1<↑UCL|/max (UCL)<0.6, red: |UCL|/max (UCL)<0.1. The lower threshold value of 0.1 is arbitrarily chosen while the determination of the upper threshold of 0.6 will be discussed in Example 1, § 5. The degree of ambiguity and arbitrariness in the evaluation of our final result of interest, the mobility parameter, is detailed in Example 2, § 1.3, with the relative uncertainty typically within ±3%.
The motion of the contact line in response to cyclic excitation is shown in six snapshot schematics in
In
In the schematic version of the cyclic diagram,
Remarkably, in the cyclic diagram the wing regions map to a single region passing through the origin, well approximated as linear. Note that the formation of this linear region is independent of any colouring scheme; it serves as the basis for identifying the wing region in the traditional diagram. The slope of this line represents a property of the traditional diagram since the same weighting factor, η, is applied to both axes and thereby preserves the original information in the TD. This property, measured as the slope Λ, is what we call the CL drag resistance or drag coefficient (inverse mobility), cf.
The interpretation of the two cyclic diagram loops is immediate. Start at the top of the red region in
Mobility characterizes how CL speed {dot over (η)} relates to CA deviation, Δα≡α−
The slope of ηΔα versus ηUCL characterizes the resistance to CL motion,
ηΔα=ΛηUCL. (6.1)
In view of the mobility, M≡1/λ, limits M→0 (Λ→∞) describe a pinned CL and M→∞ (λ→0), a fully mobile CL, as mentioned in Example 1, § 5. We shall report Λ values below. In the absence of a molecular basis for scaling Λ, we will scale empirically using length D, time τ* and angle deviation Δα*, as provided in Table 1.
Mobility 1/Λ is measured by doing a best fit of (6.1) to the wing data, using as a free parameter. The best fit to the data of
One might expect that advancing and receding CLs wings, in general, could have different mobilities. This could well be the case if ā is set to be an independently determined (or assumed) value. In place of
In this example, we eschew the need for any additional information or assumptions by contenting ourselves with an overall mobility characterization for both the advancing and receding regimes. The M00 system lends itself to this approach with its low hysteresis that makes it naturally symmetric (φ˜0). Our 1-parameter fit procedure is equivalent to minimizing angle φ in
Various response diagrams have been introduced in order to study the moving contact line during inertial-capillary wetting/unwetting motions. Each highlights different features.
The platform phase plane serves as a clock. It yields the fractions of the driving period that the motion spends in stick and wing regions. The mixing of colours indicates the relative regularity of the various regime transitions. There is some mixing at each transition yet the stick-slip and slip-stick transitions exhibit the most mixing,
The CL phase plane reflects how the droplet filters the driving motion to the CL motion. Both amplitude and phase of the mapping from platform to CL motion carry information. Remarkably, amplitudes η are of the same order as amplitudes X while UCL is 2-fold greater than {dot over (X)}, a benefit of resonance. The advancing wing (wetting) is more regular with greater amplitudes than the receding wing (unwetting), as noted by prior studies (e.g. Elliott & Riddiford 1967). Regarding phase difference, maximum speeds on advancing and receding wings both occur before platform maximums. New here is a means to measure the differences in regularity, with the benefit of multicyclic statistics. In summary, the mapping from the platform to the CL phase plane is a new and useful characterization of CL motions.
The mixed diagram,
The CL cyclic diagram is distinguished by its quadratic nature. The axes in this diagram are scaled to bring the sweeping of the CL past the rest position into focus. The wing regions map to a linear segment whose inverse slope yields the mobility measurement. Definition of the wing regions, alternatively, could be specified in the cyclic diagram. The surprise then is that (i) the wing regions are linear to a good approximation and (ii) the linearity corresponds to a major fraction of the driving cycle.
How is mobility influenced by the support affinity? An F00 system exhibits greater hysteresis, αA−αR, and a higher static CA, Table 4 and Λ doubles from the M00 value, Table 5. This greater resistance to mobility is consistent with the higher hysteresis due to surface chemistry. For the various F00 diagrams, see Example 2, § 2 and
The breadth of usefulness of the cyclic diagram (and dynamic balancing procedure) depends on the extent to which mobility is a material-like parameter, like viscosity given by a rheometer and used to make predictions in other flow geometries and contexts. This important consideration is beyond the scope of this example. However, a necessary condition is that measured mobility parameters for driving drops near resonance be independent of details of our cyclic-dynamic protocol. Next, we argue this point.
TABLE 5. Measured λ and M for Mxx and F00 systems. αα*τ*/A*=17 s cm−1.
To what extent is mobility independent of V and a? Capillary resonance depends on drop volume and large volumes invoke gravity. Additionally, higher accelerations distort shapes and influence CL behaviour. Minimal influence of gravity on capillarity is ensured by Bo≡ρgD2/σ<<1, and on driving acceleration by g/a<<1, both limited by extreme shape distortions that come with higher accelerations that ultimately result in atomization.
For the M00 system, measured values of Λ at varying driving acceleration and drop sizes are given in
We experimentally study the motion of contact lines (CL) by driving a sessile water drop near resonance. The motions conform to classical CL behaviour, by the traditional diagram (TD). We then use the TD to identify stick and wing regions. The stick region starts (ends) at the onset of sticking (slipping) on a receding (advancing) CL. By colouring the data by region, one can observe how the TD maps to the CL cyclic diagram. For water on a neutrally wetting and low-hysteresis support, the cyclic diagram reveals a linear response of wing data which yields the CL mobility measurement.
Any system of partially wetting liquid and support can be tested by the procedure introduced here. Wing regions can be anticipated—they appear routinely in the nearly 50 years of reporting data in the TD format. Hence, our approach is of broadest applicability. What cannot be anticipated is a successful mobility measurement from the cyclic diagram.
Demonstrating how to measure mobility suggests a way around the long-standing difficulty, by way of reinterpretation, that systems that display CA hysteresis do not have a well-defined linearized stability theory (Davis 1983). Mobility measurement has been demonstrated for water on support M. This is a ‘sweet spot’ in parameter space. Mobility decreases from this sweet spot for system F00, owing to increasing CA hysteresis. Mobility also decreases from the F00 value with increasing bulk viscosity,
A number of open questions remain. How far from the sweet spot in parameter space will the dynamic CA procedure still successfully yield a mobility measurement? To what extent is mobility a material-like parameter (as mentioned)? Finally, to what extent can theory account for the sweet spot and predict the mobility values?
In summary, the introduced diagrams reveal a wealth of information about rapidly moving CLs and subsume the TD. All the features from the TD, including α, αA, αA′, αR, αR′ near the stick-slip boundary, can be extracted. In much the same way, the dynamic CA goniometer subsumes the traditional goniometer, using measurements that are cyclically averaged. The information revealed is highlighted by the cyclic diagram remapping which, in conjunction with the cyclic measurements, enables the mobility to be measured. To the inventors' knowledge, this procedure has yielded the first direct, experimental measurement of mobility for rapid CL motions.
Example 2 provides supplemental material relating to the experimental information described in Example 1.
Since velocity is estimated as the numerical time derivative of position measurements based on a central differencing scheme, the absolute error in velocity can be shown to be approximately
δV=δx/(√{square root over (2)}Δt), (1.1)
where δV and δx are the uncertainties in velocity and position, respectively, while Δt is the time step between consecutive frames.
Having incorporated a sub-pixel edge detection algorithm (Trujillo-Pino et al. 2013), δx is expected to be smaller than a pixel but its approximate size is not immediately available. On the other hand, an approximation for δV can in fact be obtained by examining the CA-UCL plot in
An industrial practice for the calibration of CA measurements is to use a solid sphere partially visible above a horizontal substrate. The contact angle between the image of the sphere and the substrate can then be measured optically and verified against calculations based on known geometry (First Ten Angstroms 2004). In order to isolate the uncertainty of our CA measurement algorithm, a synthetic image of a circle was used instead. The CA values as measured by image analysis are compared against analytically determined values and the errors are between −1.5° to 0.5° over the range of CA values relevant to this work.
As A is a derived quantity based on statistical analysis, the random error in Λ can be reduced simply by collecting data over longer times. Therefore, the most significant contribution to the uncertainty in Λ comes from the two free parameters used in its evaluation. The first parameter is the assumed value of the equilibrium contact angle, α, which affects the alignment between the advancing and receding parts of the linear region in the double-loop diagram. The second parameter is the threshold velocity value, Uthresh, that determines the boundaries of the linear region.
For α, an unambiguous maximum can be found in the R-squared value of the linear fit to the linear region, at a particular value of Uthresh. This value of α that maximizes the R-squared value is used in our evaluation of Λ. Varying Uthresh over a range of reasonable values produces a values within about 0.4°, with negligible impact on the final evaluation of Λ.
For Uthresh, there is indeed some ambiguity about where exactly the linear region ends and the transition regions begin. However, choosing a value that clearly includes some of the transitional data points or clearly excludes some data in the extremities of the linear region results in a spread of Λ values within ±3%.
Water has i) a high surface tension with low viscosity and water on M exhibits ii) a rest state CA near 90° with iii) a low CA hysteresis. Choice i) favours underdamped vibrations and the inertial-capillary balance. Choice iii) favours a shorter sticking duration (26%, c.f.
The F00 system exhibits greater CA hysteresis and a more phobic rest state CA, Table 4. Shown in
Owing to greater hysteresis of the F00 system, more time per driving period is spent in the stick region. For a similar reason, there is more mixing of colours. The F00 diagram (see
Citation of a reference herein shall not be construed as an admission that such reference is prior art to the present invention. All references cited herein are hereby incorporated by reference in their entirety. Below is a listing of various references relating to the present disclosure:
Illustrative embodiments of the processes, methods, and products of the present disclosure are described herein. It should be understood, however, that the description herein of the specific embodiments is not intended to limit the present disclosure to the particular forms disclosed but, on the contrary, the intention is to cover all modifications equivalents and alternatives falling within the spirit and scope of the invention by the appended claims. Thus, although the present invention has been described for the purpose of illustration, it is understood that such detail is solely for that purpose and variations can be made by those skilled in the art without departing from the spirit and scope of the invention which is defined by the following claims.
This application claims priority benefit of U.S. Provisional Patent Application Ser. No. 62/534,147, filed Jul. 18, 2017, the disclosure of which is hereby incorporated by reference herein in its entirety.
This invention was made with Government support under Grant Numbers 1236582 and 1637960 awarded by the National Science Foundation. The Government has certain rights in the invention.
Number | Name | Date | Kind |
---|---|---|---|
9279435 | Bohringer | Mar 2016 | B2 |
10525472 | Pandey | Jan 2020 | B1 |
20100024529 | Dillingham | Feb 2010 | A1 |
20140144518 | Bohringer | May 2014 | A1 |
20190022655 | Holmes | Jan 2019 | A1 |
Number | Date | Country |
---|---|---|
2012032258 | Feb 2012 | JP |
Entry |
---|
Zhang Shi et al., “Dynamic contact angle hysteresis in liquid bridges,” Colloids and Surfaces A: Physicochemical and Engineering Aspects, 555:365-371(2018) (Abstract only). |
Hun Kim et al., “Mode pattern of internal flow in a water droplet on a vibrating hydrophobic surface,” J. Physical Chemistry, 119(22):6740-6746 (2015) (Abstract only). |
Robert H. Temperton, “Resonant vibrations of microlitre liquid drops,” Thesis submitted to the University of Nottingham for the degree of Master of Science (by Research), 116 pages, The University of Nottingham (2012). |
James S. Sharp et al., “Contact angle dependence of the resonant frequency of sessile water droplets,” Langmuir, 27 (15):9367-9371 (2011) (Abstract only). |
Srinivas Mettu et al., “Motion of Liquid Drops on Surfaces Induced by Asymmetric Vibration: Role of Contact Angle Hysteresis,” Langmuir, 27(16):10327-10333 (2011) (Abstract only). |
Paolo Sartori et al., “Drop motion induced by vertical vibrations,” New Journal of Physics, 17:113017:1-15 (2015). |
Xavier Noblin et al., “Vibrations of sessile drops,” Eur. Phys. J. Special Topics, 166:7-10 (2009). |
Aditi Chakrabarti et al., “Vibrations of sessile drops of soft hydrogels,” Extreme Mechanics Letters, 1:47-53 (2014). |
Susan Daniel et al., “Vibration-Actuated Drop Motion on Surfaces for Batch Microfluidic Processes,” Langmuir 21:4240-4248 (2005). |
Yi Xia and Paul H. Steen, “Moving contact-line mobility measured,” J. Fluid Mech. 841:767-783 (2018). |
Number | Date | Country | |
---|---|---|---|
20190025177 A1 | Jan 2019 | US |
Number | Date | Country | |
---|---|---|---|
62534147 | Jul 2017 | US |