Automatic Single Droplet Generator with Control over Droplet Size and Detachment Frequency - MDPI
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colloids and interfaces Article Automatic Single Droplet Generator with Control over Droplet Size and Detachment Frequency Dorota Gawel and Jan Zawala * Jerzy Haber Institute of Catalysis and Surface Chemistry, Polish Academy of Sciences, 00-901 Krakow, Poland * Correspondence: nczawala@cyfronet.pl; Tel.: +48-6395-133 Received: 7 August 2019; Accepted: 20 August 2019; Published: 22 August 2019 Abstract: This paper presents a quite simple, fully automatized single droplet generator, which can be an alternative for more expensive and complicated microfluidic devices. The simple generation nozzle connected to the pressure cells and cheap peristaltic pumps, synchronized via developed software with simple GUI (graphical user interface) implemented into the Raspberry Pi microcomputer allows precise control over the single droplet diameter and detachment frequency. The generator allows the formation of droplets of quite wide range of diameters without the need of orifice diameter replacements. Free control over time available for adsorption of surface active-substances over the surface of immobilized droplet, before its detachment from the orifice, is an advantage of the developed device. Keywords: dispersion; droplet; velocity; generator 1. Introduction The behavior of droplets dispersed in the liquid phase has great importance in many diverse industrial and technological applications, such as extraction of liquid-liquid mixtures or emulsions formation, waste-water treatment or hydrometallurgy. Efficiency of many of these applications can be investigated and partially predicted on the basis of results of fundamental studies related to the hydrodynamics of single droplets in a liquid phase. In laboratory practice, for proper experimental investigations of rising droplet hydrodynamics as well as collisions between droplets and formation of single emulsion films under dynamic conditions, control over the formation of a single droplet with the desired diameter and detachment frequency is of crucial importance. Nowadays, microfluidic devices, for which fabrication and modification has been extensively studied and described [1–6], are the most widely used for single droplet generation in a liquid phase. In such devices two immiscible liquids are pumped through microchannels, where one phase is dispersed in the other. For the sake of efficient device design and control on the size and monodispersity of generated microdroplets, many researchers have investigated various microfluidic methods of droplet generation both experimentally and numerically [1–16]. According to the mechanism of dispersion, microfluidics devices can be divided into three groups: devices where a droplet is formed as a result of (i) breakup in co-flowing streams [4,5,7,10]; (ii) breakup in cross-flowing streams (T-junction) [9–12]; and (iii) breakup in elongational strained flows (flow-focusing) [14–16]. The undoubted advantage of microfluidic devices (called microchips) is their ability to generate single droplets with micrometer size. Furthermore, such devices are usually small and handy. However, the size range of generated droplets depends on the microchannels diameter. Moreover, the microchannels diameter affects a single droplet velocity inside the channel as a result of droplet-wall interactions [1,5,9,17–19]. Droplet size strictly depends on microchannel geometry (for example channel length, nozzle to orifice distance etc.) [5], which should be precisely controlled for sufficient repeatability of the results. In addition, the microchips have limited mechanical durability and defined shape, which limits its applicability Colloids Interfaces 2019, 3, 57; doi:10.3390/colloids3030057 www.mdpi.com/journal/colloids
Colloids Interfaces 2019, 3, 57 2 of 9 Colloids Interfaces 2019, 3, x FOR PEER REVIEW 2 of 9 infor laboratory sufficientexperiments repeatabilityconcerning the motion of the results. of a single In addition, droplet from the microchips thelimited have very beginning mechanical of its formation and acceleration in liquid column. durability and defined shape, which limits its applicability in laboratory experiments concerning the The of motion paper presents a single dropletanfrom alternative the verymethodology beginning of its offormation single droplet generation in and acceleration inliquid the liquid column.phase. We have developed a quite simple, fully automatic single droplet generator, The paper presents an alternative methodology of single droplet generation in the liquid phase. allowing precise control over We the havesingle droplet developed diameter a quite simple,andfullydetachment automatic single frequency. Our automatized droplet generator, allowing generator allows precise control formation over the of droplets single in quite droplet wide range diameter of diametersfrequency. and detachment with very Our goodautomatized precision without generatorneedallows of orifice formation diameter of droplets in replacements. quite wide Moreover, therange time of diameters available for with very good adsorption precision of surface without need of active-substances over orifice diameter replacements. Moreover, the time available for adsorption the immobilized droplet, before its detachment from the orifice, can be precisely and easily controlled, of surface active- assubstances well as the over the immobilized degree of adsorption droplet, beforeat coverage itsliquid/liquid detachment from the orifice, interface. Thiscan be precisely feature and is important easily controlled, especially as well as the for investigations degree ofofadsorption of stability coverage single emulsion at liquid/liquid films formed under interface. dynamic Thisconditions feature is important (kinetics especially of droplet for investigations of stability of single emulsion films formed under dynamic coalescence). conditions (kinetics of droplet coalescence). 2. Materials and Methods 2. Materials and Methods 2.1. Experimental Set-Up 2.1. Experimental Set-Up All the experiments were carried out using a single-droplet generator, which was fully developed and builtAll in theour experiments laboratory. were Thecarried out using experiments werea single-droplet aimed to testgenerator, whichprecision the generator was fully anddeveloped potential and built in our laboratory. The experiments were aimed to test the in a single droplet generation of desired size. The schematic illustration of the main parts generator precision and potential of the in a single device droplet in is presented generation Figure 1a.of It desired consists size. of The schematic (i) two illustration identical, of the main programmable, lowparts of theperistaltic pressure device is presented pumps (DC 12 inV, Figure flow1(a). rateIt20-60 consists of (i) two mL/min identical, with siliconeprogrammable, tubes of 2 mm low pressure inner peristaltic diameter) pumps to connected (DC 12 V, flow rate 20-60 mL/min with silicone tubes of 2 mm inner diameter) connected to (ii) two (ii) two glass pressure cells (height 70 mm and width 35 mm, round cross-section) and controlled glass pressure cells (height 70 mm and width 35 mm, round cross-section) and controlled via dual via dual stepper motor driver (L298N, Induino ST1112); (iii) three pressure sensors (GY-68 BMP180, stepper motor driver (L298N, Induino ST1112); (iii) three pressure sensors (GY-68 BMP180, I2C); (iv) I2C); (iv) two polytetrafluoroethylene (PTFE) two-way valves, automatized using the servomechanism two polytetrafluoroethylene (PTFE) two-way valves, automatized using the servomechanism (Giant (Giant Servo HD-1235MG); (v) two pressure stabilizers; (vi) glass tube with side-tube (cross-Section Servo HD-1235MG); (v) two pressure stabilizers; (vi) glass tube with side-tube (cross-Section 8 mm,) 8 mm,) andsteel and thin thin needle steel needle (outer(outer diameter diameter 0.3 mm) 0.3 sealed mm) sealed concentrically, concentrically, referred referred furtherfurther in the in theastext text asgeneration generationnozzle, nozzle, as well as (vii) Raspberry Pi 3 microcomputer for control and synchronization of all of as well as (vii) Raspberry Pi 3 microcomputer for control and synchronization allelectronic electronicparts of thethe parts of generator generator by means by means of developed of developed software software with user-friendly with user-friendly GUI (graphical GUI (graphical user user interface), interface), presented presented in more in more detaildetail in Appendix in Appendix A. A. (a) (b) Figure1.1.Schemes Figure Schemesof:of: (a) (a) Single Single droplet droplet generator; generator;(b) (b)Experimental Experimentalset-up used set-up to to used study thethe study single single droplet size and its motion parameters. droplet size and its motion parameters. Thefollowing The followingprocedure procedurewas wasapplied appliedtotogenerate generateaasingle singleoil oildroplet dropletininwater. water.First, First,the thetwo-way two- way valves of the pressure cells (Cell 1 and Cell 2) were closed and the cells were filled with valves of the pressure cells (Cell 1 and Cell 2) were closed and the cells were filled with corresponding,
Colloids Interfaces 2019, 3, 57 3 of 9 immiscible liquids directly from the beakers. Next, the cells were pressurized independently by two peristaltic pumps according to the precisely adjusted (using software) pressure values (P1 and P2 ). These pressures were in fact overpressures, normalized to zero at the beginning of the procedure, according to the ambient pressure measured by the third, independent sensor (P3 ). Tubes used for cells pressurization were made of silicone (inner diameter 2 mm). Chemically resistant PEEK (polyether ether ketone) tubes (inner diameter 0.7 mm) were used for oil transport from the cell, through the PTFE valves to the generation nozzle. In the case of water, a PTFE tube with inner diameter 2 mm was applied. When the desired pressure values were reached independently in each cell, two-way valves of the both cells were open to fill the tubes with respective liquids, which were pumped thanks to the overpressure inside the cells. Correct, adjusted overpressure in the cells were continuously controlled and supplied, if necessary, by the peristaltic pumps. The procedure of system filling was monitored visually by observation of the air bubbles appearing inside the generation nozzle at the needle tip and continued till all air was pushed out and the first oil droplet appeared and detached from the needle tip, which indicated that the needle is filled with oil and both PTFE valves can be closed. To generate the single droplet the PTFE valve of the oil cell (Cell 2) was opened and then immediately closed. Time between valve opening and closure could be precisely adjusted. This was a very important parameter, determining the size of the droplet formed at the needle tip. After formation under the impulse of the oil phase flow of adjusted amplitude (pressure), the droplet was immobilized at the needle, as capillary force related to the needle/droplet attachment area exceeded buoyancy. To detach the droplet, water co-flow was applied. The droplet detachment was forced using water flow impulse generated from the water cell (Cell 1) to the side tube of generation nozzle. Magnitude of this impulse (and hence water flow rate and, consequently, shear force exerted at the droplet surface) depended on P1 value. In practice, the water impulse was adjusted carefully to be as small as possible, to avoid significant droplet deformation during too violent forced detachment. After each oil or water impulse, the peristaltic pumps supplied the pressure to the desired (adjusted) level. The pressure inside the cell could be freely modified, either up or down, by peristaltic pumps operating in pumping (forward pump rotation) or withdrawing (backward pump rotation) modes. To measure the droplet size and rising velocity, the generation nozzle was connected to the square glass column, according to the scheme presented in the Figure 1b. Each water impulse generated to detach a droplet caused an increase in the water level inside the liquid column, which modified the hydrostatic pressure. Therefore, a small side silicone tube was connected to the bottom of the column to keep the water level constant and controllable. Pictures of a single droplet detaching from the needle tip and rising in water were recorded using high-speed camera (with relatively low frequency applied, equal to 100 Hz). To extract the droplet motion parameters (rising velocity, shape deformation) and its size, well-known procedures, described in details elsewhere [20], were utilized. In this procedure the Python (programing language) script for automatic and fast image analysis was used. Terminal velocity was calculated as an average from five independent runs (five different droplets) for data collected at the distance when a droplet velocity was constant. Equivalent droplet diameter was calculated assuming an ellipsoidal droplet shape, as: q 3 d= dh 2 dv (1) where dh and dv is horizontal and vertical diameter. 2.2. Materials Dodecane oil was used for testing the generator potential and precision. We used contaminated dodecane available in our laboratory, with water/oil interfacial tension equal to 33 mN/m. We decided to do so, because, for preliminary tests of the generator capability, the system purity was an insignificant parameter. Milli-Q water with surface tension 72.4 mN/m was used in all the experiments, which were carried out at a room temperature equal to 22 ± 1 ◦ C.
Colloids Interfaces 2019, 3, 57 4 of 9 Colloids Interfaces 2019, 3, x FOR PEER REVIEW 4 of 9 3. Results and Discussion Colloids Interfaces 2019, 3, x FOR PEER REVIEW 4 of 9 3. Results and Discussion 3. A sequence Results and of photos showing moment of a single droplet detachment from the needle tip are Discussion presented A sequence in Figureof2.photos showing The first photo moment presents of thea elongated single droplet detachment droplet shape, which from theis aneedle tip are of consequence A sequence presented in Figure of photos 2. The showing first photo moment presents ofthe a single droplet elongated detachment droplet shape, from the which is a needle tip are consequence the shear flow of water (generated impulse) parallel to the needle. The detached droplet starts to rise presented inflow Figure 2. The(generated first photo presents parallel the elongated droplet shape, which is a consequence as of the shear a result of buoyancy. of water Please note thatimpulse) due to the carefully to the needle.magnitude adjusted The detached droplet of the water starts to shearing of the shear rise as the a result flow of water of buoyancy. (generated Please impulse) notedisturbed, parallel that due towhich to the the carefully needle. The adjusted detached droplet starts to impulse, droplet shape is only slightly is positive featuremagnitude of the method, of theespecially water rise as shearing a result of impulse,ofthe buoyancy. Please note that due to the carefully adjusted magnitude of the water when the influence thedroplet adsorptionshapelayer’s is onlyexistence slightly at disturbed, the oil/water whichinterface is positive feature of the is investigated. It is shearingespecially method, impulse, when the droplet the shape of influence is the only slightly disturbed, adsorption layer’s whichatisthe existence positive oil/water feature of the interface worth mentioning here that such methodology of single droplet generation allows precise and is free method, especially investigated. It isof whenmentioning worth the influence here ofthat the adsorption such methodologylayer’s existence of single at the oil/water droplet generation interface allows is control over investigated. time a It iscontroldroplet worth over residue mentioning at the needle tip. Therefore, this method is a great tool for precise and free time of here that such a droplet methodology residue at the needle of single droplet generation tip. Therefore, this method allows is a investigation precise and of influence control of time available for adsorption of thesurface-active substances thisatmethod liquid/liquid great tool forfree investigation over time of a droplet of influence residue atfor of time available needle tip.ofTherefore, adsorption surface-active substances is a interface great on tool droplet for motion investigation parameters, of influence as of well time as stability available for of single adsorption thin offilms formed, surface-active when the oil substances at liquid/liquid interface on droplet motion parameters, as well as stability of single thin films formed, droplet reaches theinterface at liquid/liquid upper liquid surface on droplet (liquid/air, liquid/liquid asorstability compound interfaces). Informed, addition, when the oil droplet reaches the motion upper parameters, liquid surface as well(liquid/air, of single liquid/liquid thinorfilms compound thiswhen method the canoil be easily reaches droplet adjustedthe to produce upper water surface liquid drops falling in oil as (liquid/air, continuous or liquid/liquid phase for study compound interfaces). In addition, this method can be easily adjusted to produce water drops falling in oil as inversed continuousemulsion interfaces). phase systems. In addition, thisinversed for study method emulsion can be easily adjusted to produce water drops falling in oil as systems. continuous phase for study inversed emulsion systems. Figure Figure 2. 2. Sequence Sequence ofof photos photos illustratingsingle illustrating singledroplet dropletdetachment detachmentfrom fromthe thesteel steelneedle needletip tipunder underthe Figure the shear 2.flow Sequence of of photos generated illustrating water impulse. single droplet detachment from the steel needle tip under shear flow of generated water impulse. the shear flow of generated water impulse. Figure3a3apresents Figure presents photos photos of ofsingle singledroplets droplets of of various sizes, various afterafter sizes, automatic imageimage automatic analysis was analysis Figure applied. Each3acolumn presents photos different presents of single subsequent droplets of various droplets sizes, after automatic positions. As seen, image analysis elaborated was software was applied. Each column presents different subsequent droplets positions. As seen, elaborated applied. determinesEach column the positionpresents different of the geometric subsequent center of droplets positions. the droplet As as well as seen, elaborated dh and aswell software software determines determines of the position thea shape position of the geometric of the geometric center of the droplet as ddvand droplet as well as dh and hdv values, values, for dv values, calculations deformation ratio (dhcenter \dv) and of dthe values. for forcalculations calculationsofofa ashape shapedeformation deformation ratio ratio (dh(d \dh \d v ) and v) and d values. d values. (a) (b) (a) (b) Figure 3. (a) Sequences of photos presenting rising droplet of different sizes after automatic analysis Figure Figure in 3. (a) 3. (a) developed Sequences Sequences of softwareof(time photos photos presenting presenting interval rising rising between dropletofofdroplet droplet subsequent different different sizesafter sizes positionsafter automatic forautomatic analysis analysis each sequence is in different); (b) Single droplet diameter as a function of overpressure inside the oil cell (servo-valveis in developed developed softwaresoftware (time (time intervalinterval betweenbetween subsequentsubsequent droplet droplet positions positions for each for each sequence sequence is different); different); (b)opening (b)0.3 Single droplet time Single droplet diameter s). asdiameter a functionas aoffunction of overpressure overpressure inside theinside the(servo-valve oil cell oil cell (servo-valve opening opening time 0.3 s). time 0.3 s).
Colloids Interfaces 2019, 3, 57 5 of 9 The pressure characteristics of the generator under experimental conditions, i.e., dependence of droplet diameter as a function of overpressure inside the oil cell (Cell 2), are presented in Figure 3b. The points represent experimentally obtained data, while the solid line is a fitted polynomial. Using fitted equation, all parameters of the generator can be easily adjusted to produce a droplet of the desired size. No error bars for diameter values are shown in the Figure for clarity. In practice, the relative standard deviation (RSD) was less than 4%. It has to be underlined that, obviously, the pressure characteristics presented in Figure 3b are valid only under certain experimental conditions, and will be different for different physical parameters of the dispersed (oil) phase, various values of interfacial tension and hydrostatic pressures (height of the liquid column). Such characteristics however, can be easily determined and catalogue for different substances as well as experimental set-up geometry, and used as a guideline (kind of “calibration curves”) during experiments performed under reproduced conditions. This is a big advantage of the method, allowing a simple way of repeating the experiments using “calibrated” systems, without blind tests. Figure 4 presents terminal velocities of a single droplet (Figure 4a) and corresponding Reynolds numbers (Figure 4b) as a function of the droplet size. Terminal velocity of every object rising (or falling) in a liquid phase is reached when the buoyant force and drag force of a continuous medium are equal. Buoyant (FB ) and drag (FD ) forces can be expressed as: FB = Vb ∆ρg (2) FD = 0.5ACD ρc u2 (3) where Vb is an object volume, ∆ρ is difference between density of dispersed (ρd ) and continuous (ρc ) phases, g is gravitational acceleration, A is object projected area, CD is drag coefficient and u is terminal velocity. In our case, due to the fact that the oil was contaminated with surface-active substances, rising droplet surface should be immobile (as a result of motion induced surface tension gradients) and can be treated as a surface of a rigid sphere. Drag coefficient of a rigid sphere can be calculated from the empirical correlation given by Schiller–Naumann [21]: 24 CD = 1 + 0.15Re0.687 (4) Re where Re is the Reynolds number, which, for the droplet of diameter d rising in continuous medium of viscosity µc can be expressed as: dρc u Re = (5) µc After rearrangement of Equations (1)–(4), assuming that the Vb is equal to 1/6πd3 and A is equal to 1/4πd2 , the theoretical droplet terminal velocity can be calculated as: 1/3 4 ρd − ρc u = gReµc (6) 3 ρc 2 CD Theoretical dependences calculated from Equations (3)–(5), according to the physical parameters of dispersed (oil) and continuous (water) phases given in Table 1, are shown in the Figure 4, as solid lines. As seen, very good agreement between experimental data and theoretical predictions was obtained. It indicates that indeed, the droplet surface was fully no-slip (immobilized). Moreover, the presented results confirm the reliability of the droplet generation method and generator itself. It is seen that using our automatic generator quite wide range of droplet size can be obtained. In practice, by using a steel needle of an outer diameter of 0.3 mm, droplets with size ranging between 600 µm to 3.5 mm can be easily produced. In addition, droplet size can be changed smoothly and continuously. The RSD of determined velocity values shown in Figure 4a was less than 5%.
be treated as a surface of a rigid sphere. Drag coefficient of a rigid sphere can be calculated from the empirical correlation given by Schiller–Naumann [21]: 24 . = 1 + 0.15 (4) where Re is the Reynolds number, which, for the droplet of diameter d rising in continuous Colloids Interfaces 2019, 3, 57 6 of 9 medium of viscosity μc can be expressed as: Colloids Interfaces 2019, 3, x FOR PEER REVIEW 6 of 9 = (5) After rearrangement of Equations (1–4), assuming that the Vb is equal to 1/6πd3 and A is equal to 1/4πd2, the theoretical droplet terminal velocity can be calculated as: ⁄ 4 | − | = (6) 3 Theoretical dependences calculated from Equations (3–5), according to the physical parameters of dispersed (oil) and continuous (water) phases given in Table 1, are shown in the Figure 4, as solid lines. As seen, very good agreement between experimental data and theoretical predictions was obtained. It indicates that indeed, the droplet surface was fully no-slip (immobilized). Moreover, the (a) (b)and generator itself. It is presented results confirm the reliability of the droplet generation method seen that using our automatic generator quite wide range of droplet size can be obtained. In practice, Figure 4. Dependence of (a) single droplet terminal velocity; (b) Reynolds numbers on droplet diameter by using a steel needle of an outer diameter of 0.3 mm, droplets with size ranging between 600 μm (points–experimentally Figure 4. Dependencedetermined of (a) single values, line—theoretical droplet terminal predictions, velocity; (b) according Reynolds numbers onto Equations droplet (3)–(5)). diameter to 3.5 mm can be easily produced. In addition, droplet size can be changed smoothly and (points–experimentally determined values, line—theoretical predictions, according to Equations (3–5)). continuously. The RSDTableof 1. determined velocity values Physical parameters of theshown in Figureand oil (dodecane) 4a water. was less than 5%. Table Title 1 1. Physical ρ, kg/m parameters µ, and of the3 oil (dodecane) Pa·swater. water Title 1 1000 ρ, kg/m 3 μ, 10−3 1 ×Pa⋅s dodecane 750 - −3 water 1000 1 × 10 dodecane 750 - As was mentioned above, the time of the opening of the PTFE valve of oil cell (Cell 2) could be As was Therefore, freely adjusted. mentioned theabove, sizethe of time of the opening the formed droplet of the PTFE could valve of oil be controlled notcell (Cell only via2)control could beof the overpressure in the cell, but it also depended on the valve opening time, when the overpressureofwas freely adjusted. Therefore, the size of the formed droplet could be controlled not only via control the overpressure in the cell, but it also depended on the valve opening time, when the overpressure constant. Figure 5 presents measured droplet diameter values for five independent runs (detached was constant. Figure 5 presents measured droplet diameter values for five independent runs droplet) for constant oil cell overpressure (15 kPa) and six different values of time of the oil cell (detached droplet) for constant oil cell overpressure (15 kPa) and six different values of time of the (Cell 2) PTFE valve opening. As seen, indeed this method of droplet size control works very well. oil cell (Cell 2) PTFE valve opening. As seen, indeed this method of droplet size control works very In practice, well. In the minimum practice, time of open/close the minimum cycle ofcycle time of open/close the valves was equal of the valves to 0.3tos, 0.3 was equal so much smaller s, so much droplet diameters smaller droplet could be obtained diameters using this could be obtained approach. using In addition, this approach. In addition,from fromthetheresults results presented presented in Figure 5, the precision of our generator can be judged. Values of the droplet diameters in Figure 5, the precision of our generator can be judged. Values of the droplet diameters formed formedin in five independent runs (under five subsequent oil and water impulses) are practically five independent runs (under five subsequent oil and water impulses) are practically identical, which identical, which indicates thatthat indicates thethe developed developedgenerator generatorisisable able to to produce monodisperse produce monodisperse droplets droplets of repeatable of repeatable sizes. sizes. This This is anisextremely an extremely important important feature feature in respect in respect to fundamental to the the fundamental studies studies on emulsion on emulsion stability, stability, single singlefilms emulsion emulsion filmsand drainage drainage and coalescence coalescence phenomenon, phenomenon, where where liquid liquid film size film is ofsize is ofimportance. crucial crucial importance. Figure Figure 5. Diameter 5. Diameter of single, of single, subsequentdroplets subsequent droplets generated generated with withconstant constantoverpressure butbut overpressure different different opening times of the servo-valve of the oil cell (Cell 2). opening times of the servo-valve of the oil cell (Cell 2).
Colloids Interfaces 2019, 3, 57 7 of 9 4. Conclusions We have developed quite a simple, fully automatized single droplet generator, which can be an alternative for more expensive and complicated microfluidic devices. The simple generation nozzle connected to the pressure cells and cheap peristaltic pumps, synchronized via developed software with simple GUI allows precise control over the single droplet diameter and detachment frequency. The generator allows the formation of droplets on demand, in quite a wide range of diameters with very good precision and accuracy without need of orifice diameter replacements. Free control over time available for adsorption of surface active-substances over the immobilized droplet (degree of adsorption coverage at liquid/liquid interface), before its detachment from the orifice, is a great advantage of the developed device. Obviously, any kind of liquids can be used as oil and aqueous phases, i.e., various kind of oils and water solutions of various substances, including surfactants can be examined. The geometry of the experimental set-up can be easily modified allowing investigations on the dynamics of falling water (or water solution) droplets in the oil phase, mimicking dynamic phenomena in the inversed emulsion systems. Author Contributions: Conceptualization, D.G. and J.Z.; methodology, J.Z.; software, J.Z. and D.G.; validation, D.G. and J.Z.; investigation, D.G.; data curation, J.Z. and D.G.; writing—original draft preparation, D.G. and J.Z.; writing—review and editing, J.Z. and D.G.; visualization, J.Z. and D.G.; supervision, J.Z.; project administration, J.Z.; funding acquisition, J.Z. Funding: This research was funded by National Science Centre (NCN), grant number 2017/25/B/ST8/01247. Conflicts of Interest: The authors declare no conflict of interest. Appendix A Figure A1 presents a screenshot of the GUI of the developed software, used for controlling of the droplet formation procedure and its final size after detachment. It was developed using the Tkinter Python module. The GUI window is divided into six panels. The first is used only for pumps testing and emergency stops. The second can be used for immediate pressure cells decompression. The third controls the manual procedure of the droplet generation, in which direct overpressure values for each cell can be adjusted and the oil and water flow impulses can be manually induced, when desired. The fourth panel allows it to start the automatic procedure of droplet generation. Again, cells overpressure can be adjusted here together with precise value of the time interval between oil and water flow impulses (in the case presented in Figure A1 equal to 40 s), which correlates with the droplet detachment interval. The algorithm was developed in such a way that the oil impulse is generated after 10 s from the automatic procedure initiation and the water impulses after the adjusted time interval. After the water impulse, all procedures start automatically from the beginning. This approach is useful, when good statistics are desired, especially in experiments aimed to measure single emulsion film stability (droplet lifetime at upper liquid interface in the column). Currently, automatic detection of the droplet lifetime at the water/oil interface is under development. The fifth panel controls the opening times of the servo PTFE valves. The last one is used for manual opening and closure of the PTFE valves and is usually used for system cleaning and filling.
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