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Study of the effect of surface wettability on droplet impact on spherical surfaces

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The effect of surface wettability on droplet impact on spherical surfaces is studied with the CLSVOF method. When the impact velocity is constant, with the increase in the contact angle (CA), the maximum spreading factor and time needed to reach the maximum spreading factor (tmax) both decrease; the liquid film is more prone to breakup and rebound. When CA is constant, with the impact velocity increasing, the maximum spreading factor increases while tmax decreases. With the curvature ratio increasing, the maximum spreading factor increases when CA is between 30 and 150°, while it decreases when CA ranges from 0 to 30°.
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International Journal of Low-Carbon Technologies 2020, 15, 414–420
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doi:10.1093/ijlct/ctz077 Advance Access publication 20 January 2020 414
Study of the eect of surface wettability on
droplet impact on spherical surfaces
..............................................................................................................................................................
Xiaohua Liu1,*, Kaimin Wang1,YaqinFang
1,R.J.Goldstein
2and Shengqiang Shen1
1Key Laboratory of Ocean Energy Utilization and Energy Conservation of Ministry of
Education, School of Energy and Power Engineering, Dalian University of Technology,
116024, Dalian, China; 2Department of Mechanical Engineering, University of Minnesota,
MN 55455, Minneapolis, USA
............................................................................................................................................
Abstract
The eect of surface wettability on droplet impact on spherical surfaces is studied with the CLSVOF method.
When the impact velocity is constant, with the increase in the contact angle (CA), the maximum spreading
factor and time needed to reach the maximum spreading factor (tmax)bothdecrease;theliquidlmismore
prone to breakup and rebound. When CA is constant, with the impact velocity increasing, the maximum
spreading factor increases while tmax decreases. With the curvature ratio increasing, the maximum spreading
factor increases when CA is between 30 and 150,whileitdecreaseswhenCArangesfrom0to30
.
Keywords: droplet impact; surface wettability; spreading factor; impact velocity; curvature ratio
Corresponding author:
lxh723@dlut.edu.cn
Received 06 September 2019; revised 23 November 2019; editorial decision 10 December 2019; accepted 10
December 2019
................................................................................................................................................................................
1INTRODUCTION
Dropletimpactonasolidsurfaceorliquidlmoccursfrequently
in nature or industrial elds [1–4]. Droplet impact phenomenon
can be observed in the following practical applications. During
the cooling process inside a spray cooling tower, water droplets
impactontoheatedtubes.Inatricklebedreactor,whengasand
liquid droplets ow downward, the droplets impact with the cata-
lyst. In pharmaceutical manufacturing, solid particles are brought
into a reactor and impact with liquid. In an IC engine, petrol or
diesel fuel is injected onto a piston crown. Typical applications are
also found in the evaporators of the multi-eect distillation sea-
water desalination system. The seawater droplets impact outside
the surface of a horizontal tube during lm evaporation.
In 1876, Worthington [5,6] rstly conducted experiments to
observe the phenomena of droplet impacting a horizontal smoked
plate.Sincethen,drivenbytheinterestsofthephenomenaand
the importance of the phenomena in numerous industrial applica-
tions, researches on droplet impact were investigated all the time.
Kannan et al.[7] experimentally explored the droplet impact
behavior on a hydrophobic grooved surface. The result indicates
that a trough structure changes the shape of liquid lm spreading,
and enhancing hydrophobicity of groove surface would be more
conducive to droplet rebound. Shen et al.[8,9] did a numerical
simulation of the deformation process aer droplet impacting a
at surface. The results show that with the decrease in the contact
angle, the droplet spreading factor increases, and the oscillation
frequency of droplet slows down, reaching equilibrium sooner.
The volume-of-uid (VOF) method was applied to explore the
droplet spreading process with dierent wettability on an inclined
surface. Under the same conditions, a non-wetting surface results
in partial crushing of droplet. Li et al.[10,11] experimentally
studied the droplet impact process with dierent temperatures
(50–120C) and wettability. Results indicate that on part of
hydrophobic surfaces, the droplet retract height increases with
surface temperature, while on hydrophilic and super-hydrophobic
surfaces, this rule disappears. The dynamic characteristics of
droplet were also studied when impacting the surface where
wettability had radial and axial symmetry gradient distribution.
Quan et al.[12] rst used a pseudopotential model of the lattice
Boltzmann method and proved that retract speed and rebound
tendency both increase with a better wettability. Antonini
et al.[13] experimentally studied surface wettability eects
on the characteristics of water droplet impact. When Weber
number is between 30 and 200, wettability aects both droplet
maximum spreading distance and spreading characteristic
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Study of the eect of surface wettability on droplet impact on spherical surfaces
time. When Weber number is higher than 200, wettability
eect is secondary because of the increase in inertial force.
The VOF method was used by Liang et al.[14] to simulate
the individual droplet dynamic behavior when droplets impact
dierent wettability surfaces with dierent impact velocities.
Calculation results show that a more hydrophobic surface leads
to droplet rebound. The maximum spreading factor increases
with the decrease in the contact angle, and the time needed to
reach the maximum spreading factor reduces accordingly. The
dynamic characteristics of droplet impact on curved surfaces are
dierent from those on at surfaces. Experimental and theoretical
investigations of the impact of a droplet onto spherical target
were conducted by Bakshi et al.[15] during which spatial and
temporal variation of lm thickness on the target surface was
measured. When the target size is increased with respect to the
droplet size, the lm thinning process is slower with a larger value
of residual thickness. Mitra et al.[16] completed a theoretical
and experimental study on the eect of a spherical surface with
high thermal conductivity on the super-cooled droplet impact
process. Liang et al. [17] observed the phenomenon of liquid
drop impact on wetted spherical surfaces at low impact velocity,
using a high-speed camera. Experimental observations showed
that the drop rebound and partial rebound phenomena may
occuratlargeviscosityandlowimpactvelocity,whichcannot
be observed at small viscosity. Wang [18] studiedtheeectofthe
contact angle on the droplet impact on dry spherical surfaces by
thecoupledlevelsetandvolumeofuid(CLSVOF)method.It
wasshownthattheincreaseinthecontactanglehindersdroplet
spreading but promotes retracting [19].Theliquidlmoscillates
when the contact angle is relatively small. The oscillation period
decreases with increasing contact angle, while it increases with
the increment in the impact velocity [20].Zhanget al.[21]
used the two-dimensional lattice Boltzmann model with multi-
relaxation time (MRT) to simulate the liquid droplet impact
on a curved target. The eects of the Reynolds number, the
Weber number and the Galilei number on the ow dynamics
were investigated. Zheng et al.[22] explored the mechanism of
dropletimpactonasphericalconcavesurfacebytheCLSVOF
method. It was found that droplet impact on a spherical concave
surface showed a smaller spread factor, earlier time of central
normal jet and larger jet velocity than the impact on a at surface.
Liang et al.[23] experimentally investigated the heptane drop
impact dynamics on wetted spheres, using a high-speed camera.
The result indicates that the sphere-drop curvature ratio can
greatly inuence the splashing thresholds. Collision of a droplet
onto a still spherical particle was experimentally investigated
by Banitabaei et al.[24] during which the eect of wettability
on collision was studied. It was found that for droplet impact
onto a hydrophilic particle, the droplet is neither disintegrated
nor stretched enough to form a liquid lm aer impact in the
entire velocity range studied. However, on a hydrophobic particle,
when Weber number achieves about 200 or larger, a liquid lm
forms aer impact. With the Weber number increasing, the
lamella length and cone angle increase accordingly. Another
main conclusion is that increasing the contact angle from the
hydrophilic to hydrophobic zone has a considerable eect on
geometry of the liquid lm and lamella formation. However,
whenthecontactangleexceedsathresholdvalueof110
,the
increase in the contact angle has little eect on lamella geometry.
A similar lamella formed aer droplet impacting a small disk was
observed by Rozhkov et al.[25] with a high-speed photography
technique. Numerical researches concerning various outcomes
during single liquid droplet impact on tubular surfaces with
dierent hydrophobicity values were carried out by Liu et al.[19]
by the CLSVOF method. When the impact velocity is constant, the
increase in the surface hydrophobicity values is detrimental to the
spreadoftheliquidlmontubularsurfaces.Thelargerthesurface
contact angle is, the more likely the droplet rebound takes place.
Chen et al.[26] conducted numerical studies on the successive
impact of double droplets on a super-hydrophobic tube, using the
CLSVOF method. The results showed that the impact model is
dominated by the impact velocity: the out-of-phase impact takes
place when the impact velocity ranges from 0.25 to 1.25 m/s, while
the in-phase impact takes place when the impact velocity ranges
from 1.44 to 2 m/s. Meanwhile, the occasion of the liquid crown
is inuenced by the impact velocity and curvature ratio.
In conclusion, the research on the droplet impacting process
had a certain foundation. However, these researches mostly
focused on at surfaces, and furthermore, parameters, such as the
impact velocity, droplet size and spherical curvature, needed to be
investigated further. In this paper, a two-dimensional numerical
simulation with the CLSVOF method is used to explore droplet
dynamic characteristics of the impacting process on spherical
surfaces. The impact velocity and curvature ratio are mainly
studied when droplets impact spherical surfaces with dierent
wettability; the degree of surface wettability is represented by the
contact angle, CA.
2PHYSICAL AND MATHEMATICAL MODEL
2.1 Physical model
As shown in Figure 1, a droplet impacts a spherical surface with a
certain initial velocity, and the impact direction is parallel with the
center line of droplet and sphere. The moment when the droplet
contacts the sphere is considered as the zero moment, tsignies
the evolution time of droplet impacting process, in milliseconds.
In addition, usignies the impact velocity, in meters per second,
the ratio of the droplet falling distance to the time interval of
which, in this paper, the impact velocity is the velocity when
droplet collide with the surface the rst time; d0signies the initial
diameter of droplet, mm; and Dis the diameter of the solid sphere,
mm. Other related parameters are dened as follows:
T=t·u/d0(1)
D=d/d0(2)
H=h/d0(3)
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X. Liu et al.
Figure 1. Aphysicalschematicdiagramofthedropletimpactonaspherical
surface.
ε=d0/D(4)
where
Tis the dimensionless time, Dis the spreading factor, dis the
liquid lm spreading diameter along the sphere, in millimeters;
His the dimensionless liquid lm central height; his the liquid
lm central height (when the liquid lm rebounds into air, h
represents the vertical distance from the highest point of liquid to
the highest point of sphere), in millimeters; and εis the curvature
ratio.
2.2 Mathematical model
In this paper, the numerical simulations are accomplished by
ANSYS Fluent 14.5 soware. Droplet impacting a spherical sur-
face is a transient process. The CLSVOF method is used by
coupling VOF with level-set methods together and the advantage
of which is that parameters describing phase interface with higher
sharpness can be given out accurately. On the basis of mass and
momentum conservation, a two-dimensional laminar axisym-
metric model and Pressure-Implicit with Splitting of Operators
(PISO) algorithm which has faster convergence speed are used.
Liquid droplet is considered incompressible, and the calculation
area is isothermal during the impact process. The droplet is water.
A non-slip boundary condition is used with constant temperature,
and the wall is considered smooth without roughness.
For the liquid, the control equations of mainstream eld are
shown as follows [27].
v=0(5)
ρ∂v
t+ρvv=−p+∇vv+(v)Tσκδ(φ)φ+ρg
(6)
where
Figure 2. The comparison of the experiment results and simulation results.
vis the velocity vector; ρis the density; pis the pressure; σis the
surface free energy; gis the gravitational acceleration; and κis the
interface curvature which can be calculated in Equation 7.
κ=∇φ
|φ|(7)
where
δ(φ)can be calculated with the following formula.
δ(φ)=1+cos(πφ/a)
2a|φ|<a
0|φ|a(8)
where
a= 1.5ω,andωis the minimum mesh size.
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Study of the eect of surface wettability on droplet impact on spherical surfaces
Figure 3. PhasediagramofdropletimpactonsurfaceswithdierentCA.
3RESULTS AND DISCUSSION
3.1 Simulation model verication
Figure 2 shows the comparison between the experimental results
from Mitra et al.[16] and the numerical results from the simu-
lation model used in this paper. The initial droplet diameter is
3.1 mm, the spherical diameter is 10 mm, the contact angle is 90
and the impact velocity is 0.431 m/s.
According to Figure 2,wecanndthattwo-dimensional
numerical simulation results are consistent with the experimental
resultsatmoststagesofdropletimpact.Atthelatertime,there
just presents a little retraction lags by two-dimensional simulation
results.
3.2 Simulation results and analysis
The phase diagram of droplets impacting spherical surfaces is
shown in Figure 3. The curvature ratio is 0.2, the impact velocity
is 0.7 m/s and CA is 60,90
, 120and 150 ,respectively.From
Figure 3, the dynamic characteristics of droplet aer impact are
dierent with dierent contact angles. With the increment in CA,
the liquid lm is more prone to breakup and rebound. When CA
is 90, center sag appears at 9.2 ms. When CA is 120,droplet
complete rebounds and forms into a gourd-shape (17 ms). When
CA is 150, complete rebound takes place, and the rebound height
is higher than that with CA of 120.
The changes of the spreading factor (D)andthedimensionless
liquid lm central height (H) under dierent surface wettability
are shown in Figures 4 and 5, respectively. The curvature ratio is
0.2, the impact velocity is 0.7 m/s and CA is 60,90
, 120and
150,respectively.
As shown in Figure 4,withthedecreaseinCA,themaximum
spreading factor (Dmax)andtmax increase. Figure 5 shows that
the greater CA is, the higher the droplet rebound height and the
longer the rebound time is. The main reason is that more energy
remains aer retraction under a larger contact angle. When CA is
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X. Liu et al.
Figure 4. The changes of Dversus Tunder dierent contact angles.
Figure 5. The changes of Hversus Tunder dierent contact angles
Figure 6. Relation between CA and Dmax under dierent impact velocities.
Figure 7. Relation between CA and tmax under dierent impact velocities.
Figure 8. Relation between CA and Dmax under dierent curvature ratios.
Figure 9. Relation between CA and tmax under dierent curvature ratios.
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Study of the eect of surface wettability on droplet impact on spherical surfaces
60, droplet partial rebound occurs aer droplet reaches Dmax,
the droplet retraction makes the droplet gather and then the
liquid lm oscillates on the surface. The spreading factor and
the dimensionless lm central height attenuate gradually during
oscillation. When CA is 90,thedropletalsopartiallyrebounds
aer droplet reaches Dmax , then complete rebound happens aer
further retract. When CA is 120or 150,completerebound
occurs aer spreading; the larger the contact angle is, the earlier
the droplet leaves from the surface.
With dierent impact velocities, the relationship between CA
and Dmax andtherelationshipbetweenCAandtmax are shown in
Figures 6 and 7, respectively. The curvature ratio is 0.2, the impact
velocities are 0.431, 0.7 and 1 m/s.
Figure 6 shows that with the decrement in CA, the maximum
spreading factor becomes greater aer droplet impact. This is
because a better hydrophilicity is benecial to droplet spread.
For the same contact angle, the maximum spreading factor
increases with the impact velocity. The reason is that the greater
initial kinetic energy helps droplet to spread further. As shown
in Figure 7, under the same impact velocity, the greater CA is,
the smaller tmax is. Under the same contact angle, the lower the
impact velocity is, the larger tmax is.
Under dierent curvature ratios, the relationship between CA
and Dmax and the relationship between CA and tmax are shown
in Figures 8 and 9, respectively. The impact velocity is 0.7 m/s, and
the curvature ratios are 0.15, 0.2 and 0.25, respectively.
As shown in Figure 8, under the same curvature ratio, the
maximum spreading factor decreases with the increase in CA.
The maximum spreading factor increases with the curvature ratio,
when CA is between 30 and 150.Thisisbecausethelargerthe
curvature ratio becomes, the greater the inuence of gravity on
the spreading process is. When CA ranges from 0 to 30,the
maximum spreading factor decreases with increasing curvature
ratio. The reason is that a better hydrophilicity promotes droplet
spread and the liquid lm can spread completely along the surface,
and then some part liquid can even gather at the bottom of the
sphere [24]. Due to high wettability of the surface and the gravity,
moreandmoreliquidwouldgatheratthebottomofthesphere
untilitbreaksup,duringwhichtheupperpartofthesphere
would expose, so the spreading factor decreases. In this case, the
increment in the curvature ratio can benet the gathering at the
bottom of the sphere, which causes the upper part of the sphere
to be exposed earlier and more quickly.
Figure 9 shows that under the same curvature ratio, with the
increment in CA, the time needed to reach the maximum spread-
ing factor decreases. Surface wettability aects both the maximum
spreading factor and spreading characteristic time signicantly
[13]. Under the same contact angle, with the increment in ε,the
time needed to reach the maximum spreading factor increases.
4CONCLUSION
Theeectofsurfacewettabilityondropletdynamiccharacter-
istics aer impacting is studied with the CLSVOF method. The
main conclusions are as follows:
(i) With the increase in CA, the liquid lm is more prone to
breakup and rebound aer droplet impact [19]. The rebound
height and rebound time increase with CA. When complete
rebound occurs, the larger CA is, the earlier the droplet rebounds
away from the surface. The maximum spreading factor and time
needed to reach the maximum spreading factor decrease with the
increment in CA.
(ii) With the increase in the impact velocity, the maximum
spreading factor increases while the time needed to reach the
maximum spreading factor decreases.
(iii) The greater the curvature ratio is, the longer the time
needed to reach the maximum spreading factor is. Within the
range of contact angle from 30 to 150,thebiggerthecurvature
ratio is, the greater the maximum spreading factor is. However,
within the range of the contact angle from 0 to 30,thebiggerthe
curvature ratio is, the smaller the maximum spreading factor is.
DISCLOSURE STATEMENT
No potential conict of interest was reported by the authors.
ACKNOWLEDGEMENTS
This work was supported by the National Natural Science Foun-
dation of China (No. 51476017) and Department of Mechanical
Engineering, University of Minnesota.
FUNDING
Prof. Shen Xiao Wei Yang the Key Program of National Natural
Science Foundation of China (NO.51936002) aer (NO.51476017).
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... Surface wettability is characterized by the contact angle between a water droplet and the surface [8] and how quickly a droplet spreads across the surface [9]. A surface is hydrophilic when its static contact angle, θ c is less than 90°, hydrophobic when θ c is between 90°and 150°, and superhydrophobic when θ c is greater than 150°(figure 1) [10]. ...
... A drop hitting a flat surface retains a circular symmetry throughout the impact process [71]. Flat surfaces with a smaller θ c have a higher droplet spreading factor (ratio of length of twodimensional wetting arc and initial droplet diameter [72]) and reach equilibrium sooner than flat surfaces with a large θ c [9]. The rate of droplet spreading becomes slower with decreasing curvature ratio (the ratio of the initial droplet diameter to the surface diameter) [73]. ...
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Rising nanoscale technologies arouse interest in investigating the impact dynamics of nanodroplets. In this work, the impact of nanodroplets on solid spheres is investigated by the molecular dynamics simulation method, to comprehensively report outcome regimes and reveal the curvature effect, in wide ranges of Weber numbers (We) from 1.5 to 235.8, diameter ratios (λ) of nanodroplets to solid spheres from 0.3 to 5, and contact angles (θ) from 105° to 135°. Five outcomes are identified, including deposition, bouncing, splash, covering, and dripping. The former three outcomes are found in the high diameter ratio range (λ > 1), showing similar dynamic behaviors with impacts on flat surfaces, whereas in the low diameter ratio range (λ ≤)1, splash disappears, and covering and dripping take place additionally. At each contact angle, the outcomes are recorded in λ-We phase diagrams. It is found that the bouncing, splash, covering, and dripping are all promoted by decreasing diameter ratios; in addition, the critical Weber numbers for trigging bouncing and splash increase with decreasing θ. However, the critical We of the boundary between the bouncing to other regimes in the low diameter ratio range is not sensitive to wettability owing to the relatively small diameter of solid spheres. For quantitatively describing the curvature effect, the boundaries between the deposition and bouncing regimes in the high diameter ratio range and between the bouncing and other regimes in the low diameter ratio range are established. Both the established models show satisfactory agreement with the boundaries in the phase diagrams.
... The wetting contact occurred when the surface temperature was below or close to the saturation temperature, while non-wetting contact was observed when the surface temperature exceeded the saturation temperature. Liu et al. 35 examined the effect of surface wettability on dynamic droplet characteristics using the volume of fluid method. They compared their findings with the experiments conducted by Mitra et al. 34 This approach involved combining the VOF method with level-set techniques, allowing for a more accurate determination of the phase interface parameters. ...
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... It was found that when the impact velocity was constant, the maximum expansion factor and the time required to reach the maximum expansion factor decreased with the increase of contact angle. 33,34 Banks et al. studied the process of spray droplets impacting the solid surface and found that the kinematic viscosity, impact velocity, and surface tension effect of droplets played an important role in the oscillation. High viscosity droplets often stopped oscillation faster than low viscosity droplets. ...
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The droplet impact process on a conical tip is one of the key problems in the field of fluid mechanics and surface and interface science. This study examines the impact process of water droplets on the conical tip using experimental, numerical, and theoretical approaches. The volume of fluid method and the dynamic contact angle model are used and validated by comparing the numerical and experimental results in both the present work and literature. The effects of the Weber number, contact angle, and cone angle on the droplet behavior, especially the maximum spreading factor, are investigated. The findings indicate that the maximum spreading factor becomes larger at a larger Weber number, a smaller contact angle, and a cone angle. Based on energy conservation, two theoretical models considering the film and ring profiles are proposed to describe the droplet maximum spreading factor. The film and ring models are recommended for use when the maximum spreading factor is below and above 2.4, with the relative deviation of all calculated data less than ±18%. This study enhances the understanding of droplet impacts on complex surfaces and provides valuable guidance for engineering applications.
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Droplet impact is a common but significant phenomenon in industry. The CLSVOF (coupled level set and volume-of-fluid) method is used to numerically study the successive dual-droplet impacting a super-hydrophobic tube. For the impact velocity of 1.0 m/s, the effect of the eccentric distance on dynamic characteristics is analysed, the corresponding eccentric distances are 0.5, 1.0 and 2.0, respectively. In addition, the break-up during rebound is analysed with velocity field and pressure nephogram. Results show that, the eccentric distance hinders the spread during the initial period of spreading. With the increase in eccentric distance, more liquid gathers at the eccentric side and the liquid film might rebound easily without break-up under the same impact velocity. The break-up during rebound mainly depends on the local airflow and pressure difference. The high-pressure zone near the solid-liquid interface moves towards the eccentric side with the increase in eccentric distance.
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In this paper, the impact of successive double droplets on a super-hydrophobic tube surface is numerically studied using a three-dimensional model by the coupled level set and volume of fluid method. The effect of impact velocity on double droplets impact under different curvature ratios is studied. With the increase in impact velocity, two kinds of impact models (out-of-phase and in-phase impact) are obtained, and the coalescent liquid film presents rebound, breakup-rebound, and splash-rebound. With the increase in the curvature ratio, the spread of the liquid film along the circumferential direction is promoted, and the rim of leading liquid film up-warp can be observed earlier. The breakup of an extending liquid film is discussed in detail under the curvature ratio of 1, which is mainly influenced by the combined effects of local negative pressure, air flow motion, surface tension, and gravity of the gathering liquid. The air entrainment occurs for the impact velocity between 0.75 m/s (We = 15.4) and 1.25 m/s (We = 42.9), while no air entrainment occurs for the impact velocity exceeding 1.5 m/s (We = 61.7). The entrapped air bubbles would cause a center breakup of the liquid film or escape from the liquid film. The escaping direction is mainly determined by the pressure distribution in the liquid film.
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The coupled level set and volume of fluid method is applied to the numerical study on the successive impact of double droplets on a super-hydrophobic tube. The impact velocity varies from 0.25 to 2 m/s. These impact processes present spread, retract, rebound, breakup and splash. The out-of-phase impact takes place with the impact velocity from 0.25 to 1.25 m/s, while the in-phase impact takes place with the impact velocity from 1.44 to 2 m/s. With the impact velocity larger than 1.25 m/s, the liquid crown presents and deforms after the trailing droplet impact, then it would gather at the film edge, rebound or break up. When impact velocities range from 1.44 to 1.5 m/s, the finger liquid film presents before the liquid crown appearing. The finger head breaks with the impact velocity of 1.5 m/s during the leading droplet spreading. The zigzag liquid film becomes more obvious for larger velocities.
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Encapsulation has received a surge of interest in the biotechnological, chemical and pharmaceutical fields and other industrial processes, owing to numerous applications such as in fluidized catalytic cracking, antenna and wire fabrication, catalytic reactions, and process industries. For example, encapsulation is a technique used to entrap active agents within a carrier material and can be achieved through impact of droplets of encapsulating material on the solid particles of active agents. Considering the importance of dynamics of drop-particle collision, which directly affects the quality of film deposition during encapsulation, the current review is presented to investigate various aspects of drop impact on dry solid spherical surfaces, which is still lacking in the existing literature and aims at encouraging more researchers to study this topic. Also, this review covers frequent examples of droplet impingement onto curved surfaces, with a focus on the latest scientific findings in droplet impacting solid spherical surfaces.
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Collision of a droplet onto a still spherical particle was experimentally investigated. The effect of droplet impact velocity and wettability of the particle surface on collision outcomes was studied (0.05 < V0 < 5.0 and θ = 70°, 90°, 118°). Compared to the literature, the range of Weber number variations was significantly extended (0.1 < We < 1146), and while focus of the previous works was on impacts in which particle is larger than the droplet (Dr < 1), the drop to particle diameter ratio in this work was larger than one. Therefore, formation of a thin liquid film, i.e., lamella, was observed due to impact of a relatively high velocity droplet onto a hydrophobic particle. Temporal variations of various geometrical parameters of collision outcomes including lamella length and lamella base diameter were investigated during the impact. It was also shown that for hydrophobic targets, the extent of hydrophobicity of the particle does not affect the lamella geometry. A comprehensive map of all the available works in drop impact on a spherical target was also provided.
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Numerical researches concerning various outcomes during single liquiddroplet impact on tubular surfaces with different hydrophobicity values are carried out using a coupled level set and volume-of-fluid method. The impact velocities studied in this paper are 0.1 m/s, 0.5 m/s, 0.94 m/s, and 1.2 m/s, respectively. The contact angles of the tube surfaces are 107°, 120°, 135°, and 153°, respectively. It is found that, when the impact velocity is constant, the increase of the surfacehydrophobicity values is detrimental to the spread of the liquid film on tubular surfaces. The larger the surface contact angle, the more likely the droplet rebound takes place. For a constant contact angle, the increase of the impact velocity is helpful to the droplet spread on a tubular surface. In the end, the mechanism of splashing and rebounding of droplet impact on a tubular surface with the contact angle of 135° is explained through the distribution of the pressure and velocity fields. The difference between the outside pressure and inside pressure of a liquid film and the location of the low pressure both have a great influence on the spread, rebound, and splash.
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A drop hitting a solid surface can deposit, bounce, or splash. Splashing arises from the breakup of a fine liquid sheet that is ejected radially along the substrate. Bouncing and deposition depend crucially on the wetting properties of the substrate. In this review, we focus on recent experimental and theoretical studies, which aim at unraveling the underlying physics, characterized by the delicate interplay of not only liquid inertia, viscosity, and surface tension, but also the surrounding gas. The gas cushions the initial contact; it is entrapped in a central microbubble on the substrate; and it promotes the so-called corona splash, by lifting the lamella away from the solid. Particular attention is paid to the influence of surface roughness, natural or engineered to enhance repellency, relevant in many applications.
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Physical and mathematical models are established to simulate a deforming and rebounding process after a droplet impacting on isothermal flat solid. The simulated results are compared with the experimental results in relative literature, and a good agreement is obtained. Therefore, the adapted model can be applied to simulate the droplet deforming morphological feature after impacting. By comparing the spreading factors at different conditions, the effects of impacting velocity and the initial contact angle on the process are analyzed.
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Dynamic behavior of an impacting water droplet was simulated with the VOF(volume of fluid)method. Droplet diameter was 2.6 mm and impacting velocity was 0.5 m·s-1.Droplet dynamic behavior on simulated, hydrophilic and hydrophobic surfaces was simulated with an impacting angle of 63°, 90°, 118°and 160°. Simulation results showed reasonably good agreement with the experiment data. Surface wettability seriously affected droplet dynamic behavior. Droplet spread well and then sticked on the hydrophilic surface. On the surface with an impacting angle of 90°, droplet partly rebounded away from the surface. While droplet totally rebounded when impacting on the hydrophobic surface. There was an edge liquid ring for liquid sticking on the droplet edge when contact line draw back. The maximum spreading factor and the time needed to arrive at the maximum spread diameter were reduced with increasing contact angle.
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The lattice Boltzmann potential model was firstly used to simulate the droplets impacting on solid surfaces. The flow state of droplets on solid surfaces and the effects of the impact parameters on the droplet impingement have been studied. It has been observed that surface wettability has a significant influence on the droplets impacting dynamics, the less of surface wettability, the easier to rebound and the faster of the recoiling speed. The higher of the impact speed and the smaller of the liquid viscosity, the bigger of the relative diameter is. In addition, the maximal relative diameter has linearity relation with the Weber number. Simulation results are consistent with the previous theory prediction and experimental results.
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In order to explore the mechanism of droplet impact on a spherical concave surface, a numerical model using the coupled level set and volume of fluid method was developed. The mechanism of droplet impact and breakup during spreading was obtained. The impact characteristics were closely related to impact velocity. Droplet impact on a spherical concave surface showed a smaller spread factor, earlier time of central normal jet and larger jet velocity than the impact on a flat surface. The maximum spread factor and relative maximum spread velocity increased exponentially with Reynolds number. The maximum length of jet increased logarithmically with Reynolds number. The maximum jet velocity decreased exponentially with Reynolds number. Through comparison of theoretical analysis models of maximum spread factor, the development direction of analysis model of maximum spreading factor of droplet impact on a concave surface was presented.