In this work, we investigate the change of contact angle (CA) of a water droplet during evaporation on a Teflon AF1600 surface in the temperature range between 20 and 80 °C under standard laboratory conditions. An almost constant initial CA and a significant increase of the stabilized CA have been observed. The results reveal a temperature-dependent CA change, mainly due to water adsorption on the solid surface. Soaking experiments indicate that besides adsorption, a temperature-independent friction-like force contributes to the pinning of triple-line and therefore to the CA change. We propose an adsorption coverage parameter and a friction-like force to describe the CA change. Furthermore, we describe a reproducible process to produce smooth and homogeneous Teflon AF1600 thin films, minimizing the influence of roughness and local heterogeneity on the CA.
In this work, we investigate the change of contact angle (CA) of a water droplet during evaporation on a Teflon AF1600 surface in the temperature range between 20 and 80 °C under standard laboratory conditions. An almost constant initial CA and a significant increase of the stabilized CA have been observed. The results reveal a temperature-dependent CA change, mainly due to water adsorption on the solid surface. Soaking experiments indicate that besides adsorption, a temperature-independent friction-like force contributes to the pinning of triple-line and therefore to the CA change. We propose an adsorption coverage parameter and a friction-like force to describe the CA change. Furthermore, we describe a reproducible process to produce smooth and homogeneous Teflon AF1600 thin films, minimizing the influence of roughness and local heterogeneity on the CA.
Wettability of a droplet
on a solid surface is an essential property
of surface science. The primary method to describe the wettability
is the contact angle (CA) measurement. The CA is defined by Young’s
equation,[1] as the angle θY at the triple-line governed by equilibrium of surface tensionswhere γ is the interface tensions, and
the subscripts s, l, and
a represent solid, liquid, surrounding air, respectively.
Changing and controlling the surface wettability and CA by microstructure-patterning
for achieving superhydrophobic surface (Lotus Effect[2]), applying voltage for manipulation of conductive liquids
on a surface (Electrowetting[3−5]), and so forth has been a research
hotspot over the last decades. However, variations from θY are observed. These variations lead to an inaccurate control
of the CA and surface wettability.Standard explanations for
the variation of CA from θY are surface imperfections,
such as surface roughness,[6] chemical heterogeneity,[7] and adsorption.[8] The
Wenzel-state has
been introduced to describe the CA on a rough surface.[9] It indicates that the surface roughness increases the hydrophobicity
if the surface is hydrophobic, that is, CA > 90°. In contrast,
roughness enhances the wettability of hydrophilic surfaces, that is,
CA < 90°. Another expansion of Young’s equation, known
as Cassie’s equation, takes the local chemical heterogeneity
of the surface into account.[10] Moreover,
molecule adsorption on the solid surface also significantly affects
the solid surface’s energy, and consequently the CA. Water
molecules can physically and chemically adsorb on all solid surfaces
with high surface energy (hydrophilic surfaces).[11] Water molecules can also adsorb onto hydrophobic materials,
like Teflon.[12−16] Lam et al.[8] experimentally demonstrate
the influence of chain length and molecule size of the liquid on the
adsorption process and therefore the CA change: the smaller the molecule
size of the liquid is, the higher is the possibility of being adsorbed
on the surface, causing a more significant CA change.The droplet
evolution during the evaporation process on solid surfaces
has been studied for years, a significant CA change from its initial
value has been observed. Usually two regimes of droplet evolution
are identified: a constant contact radius (CCR), and a constant contact
angle regime (CCA).[8,17−20] In the CCR regime, the contact
area stays constant, meanwhile, the CA decreases during droplet volume
loss by evaporation. When the CA reaches a specific value, the CCR
regime transforms to the CCA regime, in which a constant CA is observed.
Therefore, two distinct values of the CA are identified: the initial
CA, and the receding or stabilized CA.[21,22] For inhomogeneous
solid surfaces, an additional regime of stick–slip has been
observed.[8,23]Teflon AF1600 is a amorphous fluoropolymer
based on a copolymer
of 4,5-difluor-2,2-bis(trifluoromethyl)-1,3-dioxol (PDD, 65 mol %)
and tetrafluoroethylene (TFE). It has extraordinary properties, such
as high-temperature stability,[24] outstanding
chemical resistance, and low surface energy, widely used in application
fields requiring a high water contact angle (WCA), for example, EW-based
variable focus liquid lens[4,5] and so forth. Compared
to traditional fluoropolymers, such as polytetrafluoroethylene (PTFE)
and perfluoroalkoxy alkane (PFA), which are mostly semicrystalline
or highly crystalline and only soluble in high-boiling solvents at
a temperature near their melting point,[25] Teflon AF1600 is amorphous and soluble in some fluorinert solvents
at room temperature. Because of its solubility, Teflon AF1600 can
be used to make thin and homogeneous films by various methods, including
spin coating, dip coating, and spray coating.[25,26]In this work, we investigated the WCA change on a Teflon AF1600
surface by water evaporation at various temperatures and observed
the evolution of droplets and WCA with time. We compared the WCA change
at various temperatures and conducted soaking experiments to observe
the influence of water adsorption on the WCA. From these experiments,
we concluded that the WCA change by evaporation is mainly due to a
temperature-independent friction-like force and the temperature-dependent
water adsorption on the solid surface. Finally, we proposed a compact
model to describe the WCA change.
Experimental
Details
Fabrication of Thin Film
A reproducible fabrication
process is presented to achieve smooth, pinholes-free Teflon AF1600
thin films to minimize the influence of roughness and local heterogeneity
on the CA.A 2% solution by weight of Teflon AF1600 (DuPont
Co. U.S.A.) in fluorinert FC-40 solvent (3M Company) is prepared and
stirred at 50 °C for 4 days. The solution is then filtered using
a PTFE membrane (pore size 5 μm, purchased from Sigma-Aldrich)
to remove undissolved or aggregated particles. After filtration, the
solution is placed in vacuum for a few minutes to remove air bubbles,
which are trapped in the solution or created by the filtration process.
In order to increase the adhesion of Teflon AF1600 on the solid substrate,
titanium (Ti) prime is first spun at 4000 rpm for 1 min onto a silicon
wafer (spin coater, Süß Technic) and dried at 120 °C
for 2 min. The Teflon AF1600 solution is then spun at 4000 rpm for
1 min. Next, the samples are soft-baked on a hot plate at 175 °C
for 10 min to remove the solvent, followed by two additional hard-baking
processes at 165 °C (glass transition temperature of Tefon AF1600)
and 330 °C (glass transition temperature of PDD) for 5 and 15
min, respectively. This baking procedure is the standard process proposed
by DuPont. However, pinholes have been observed on the surface after
the third baking step, seen in Figure a, and an additional stick–slip phenomenon appeared
in our preinvestigation of the WCA during evaporation.
Figure 1
(a) Optical micrograph
of a Teflon AF1600 surface: pinholes are
observed after the third baking step with 330 °C. (b) A typical
AFM image of Teflon AF1600 surface fabricated by two baking temperatures.
The mean root square roughness is 0.82 nm.
(a) Optical micrograph
of a Teflon AF1600 surface: pinholes are
observed after the third baking step with 330 °C. (b) A typical
AFM image of Teflon AF1600 surface fabricated by two baking temperatures.
The mean root square roughness is 0.82 nm.To investigate the influence of the third baking step, we used
different methods to determine the surface quality before and after
the last baking with temperature of 330 °C: Fourier-transform
infrared spectroscopy[24] (FTIR, Tensor Bruker
27, reflective spectral range of 3500–400 cm–1) for analyzing the surface functional groups (the FTIR results are
shown in Supporting Information), atomic
force microscopy (AFM, Bruker Dimension Edge, with Bruker NCHV-A cantilever
in tapping mode) for observation of surface morphology, and WCA measurement
(Krüss DSA30S, sessile droplet method) to estimate the surface
tension. These properties of the Teflon AF1600 thin film showed no
changes after the last baking step.Therefore, we have chosen
two baking steps at 175 and 165 °C
for 10 and 5 min, respectively, to achieve pinhole-free Teflon AF1600
surfaces. The average thickness 210 ± 15 nm of the Teflon AF1600
film was determined by measuring the step height with a profilometer
(Dektak). The surface roughness was determined by AFM and resulted
in a mean root square roughness Rq = 0.82
nm on a scan area of 10 × 10 μm2. A typical
AFM image of Teflon AF1600 is shown in Figure b.
Experimental Setup
The contact angle
measurements are
carried out under standard chemical laboratory conditions, that is,
constant temperature of 20 ± 1 °C, atmospheric pressure
and relative humidity of 35 ± 1%. The experimental setup consists
of a drop shape analyzer (DSA, Krüss DSA30S) and a custom-built
temperature controlled test chamber (see Figure ). Images with a resolution of 200 Pixel/mm
taken from DSA are analyzed for the droplet contour. The pendant drop
method is used to measure the liquid surface tension, while the sessile
drop method is used to determine the CA.[27] The measurement resolutions are 0.01° for the CA, and 0.01
mN/m for the surface tension. At the baseplate the temperature is
precisely controlled (ΔT < ±0.01 °C)
by a Peltier element with a controller (Meerstetter TEC-1091). The
high thermal conductivity of the aluminum (Al) plate guarantees a
homogeneous temperature distribution at the baseline of the droplet
as well as at the triple-line. The Al-cover reduces the T gradient in the chamber. A groove inside the chamber, which can
be filled with water, allows to control the humidity inside the chamber
and to reduce the evaporation speed. At a chamber temperature of 20
± 1 °C the evaporation rate has been reduced from 0.16 to
0.004 μL/min.
Figure 2
Illustration of the experimental setup. (A) Front view,
(B) top
view, and (C) front view of the Al cover with glass windows and a
small opening with 2 mm diameter at the top for inserting dosing needle.
A Peltier element under the Al plate, two temperature sensors, and
a temperature controller guarantee a homogeneous temperature contribution.
For water droplet evaporation process, the Al cover (black dash line
in A) is removed to achieve atmospheric humidity and allowing droplet
evaporation. For soaking experiments to investigate the effect of
water adsorption on WCA, the groove integrated in the Al base plate
is filled with water to create an atmosphere of saturated humidity
(blue dash line in A and details seen in B), and the Al cover is placed
to maintain the saturated humidity inside the chamber.
Illustration of the experimental setup. (A) Front view,
(B) top
view, and (C) front view of the Al cover with glass windows and a
small opening with 2 mm diameter at the top for inserting dosing needle.
A Peltier element under the Al plate, two temperature sensors, and
a temperature controller guarantee a homogeneous temperature contribution.
For water droplet evaporation process, the Al cover (black dash line
in A) is removed to achieve atmospheric humidity and allowing droplet
evaporation. For soaking experiments to investigate the effect of
water adsorption on WCA, the groove integrated in the Al base plate
is filled with water to create an atmosphere of saturated humidity
(blue dash line in A and details seen in B), and the Al cover is placed
to maintain the saturated humidity inside the chamber.As evaporation experiments can last for 1000 s and more,
we preinvestigated
if contaminations of the water droplet from the surrounding air affect
measurement results. The pendant drop contour[27] was used to determine the surface tension of deionized water (DI
water, 16–18 MΩ·cm). The result showed that the
water surface tension decreased by less than 1 mN/m from 72.8 to 72
mN/m after 1500 s at laboratory condition. For our experiments this
would result in a WCA change of less than 0.5°. On the basis
of these results, we neglect the influence of contamination.Droplet evolution and spreading on solid surfaces is governed by
capillary, triple-line, and viscous force. The capillary number Ca
is used to describe the relative effects of viscous forces and surface
tension forces acting across the boundary: Ca = μ·v/γ[28] with the dynamic
viscosity of the liquid μ, the spreading velocity v of the contact line, and the liquid surface tension γ. The
maximum contact line velocity observed in our experiments results
in a maximum capillary number 7 × 10–8, which
is substantially lower than the critical value of 10–5,[29] therefore any impact of viscous force
is neglected in this work.
Results and Discussion
Contact
Angle during Droplet Evaporation
First, the
sample is cleaned with acetone and isopropanol, and then blown dry
with nitrogen to ensure a clean and dry Teflon AF1600 surface. Next,
the temperature of the base plate is adjusted. A droplet with a volume
of 5 μL is generated at the needle tip, and then slowly deposited
onto the sample surface. The WCA measurement starts after ∼1
s, when the droplet has reached its thermal equlilibrium at the sample
surface. Within the first 15 s, images of the droplet are taken every
second, and then the droplet shape evolution is monitored every 4
s. The measurements stop when the drop volume is less than 1.5 μL. Figure shows typical results
for the droplet evaporation process over time: the evolution of the
WCA, the droplet volume, and the contact area diameter at four temperatures.
It shows clearly a CCR regime followed by a CCA regime. In the CCR
regime, the triple-line stays pinned at a fixed position (constant
contact base diameter) while volume and WCA continuously decrease.
As the triple-line gets depinned and starts moving, the CCA regime
is established and the WCA stays constant while the droplet evaporates.
We extract two characteristic WCAs: the initial WCA (θinit) and the stabilized WCA (θsta). Both values are
determined from the experimental data by a linear least-square fit.
Figure 3
WCA, contact
base diameter, and droplet volume evolution due to
droplet evaporation over time at (a) T = 20 °C,
(b) T = 40 °C, (c) T = 60 °C,
(d) T = 80 °C. The solid lines represent the
fitted curves in the CCR and CCA regime. In the CCR regime, the contact
base area stays constant and the WCA decreases. In the CCA regime,
however, the contact base area decreases and the WCA stays constant.
Representative droplet images of (e) initial WCA θinit at T = 20 °C, (f) stabilized WCA θsta at T = 20 °C, (g) initial WCA θinit at T = 80 °C, (H) stabilized WCA
θsta at T = 80 °C.
WCA, contact
base diameter, and droplet volume evolution due to
droplet evaporation over time at (a) T = 20 °C,
(b) T = 40 °C, (c) T = 60 °C,
(d) T = 80 °C. The solid lines represent the
fitted curves in the CCR and CCA regime. In the CCR regime, the contact
base area stays constant and the WCA decreases. In the CCA regime,
however, the contact base area decreases and the WCA stays constant.
Representative droplet images of (e) initial WCA θinit at T = 20 °C, (f) stabilized WCA θsta at T = 20 °C, (g) initial WCA θinit at T = 80 °C, (H) stabilized WCA
θsta at T = 80 °C.Figure shows
the
initial and stabilized WCAs for the temperature range from 20 to 80
°C. The initial WCA θinit is almost constant,
changes slightly from 121.1° to 122.9°, and the stabilized
WCA θsta shows a significant increase from 113.3°
to 119.7°. This trend is also observed by Weisensee et al.,[13] who have controlled the pressure to the corresponding
temperatures. The uncertainty of the measurement of the initial WCA,
especially for temperatures >50 °C with evaporation rates
>0.02
μL/s, can be determined from the maximum measurement delay of
1 s: the measured θinit could be maximal 0.3°
smaller than the actual θinit. Moreover, the θsta at higher temperatures (T > 50 °C)
are more scattered with a standard deviation of ∼0.25°
compared to ∼0.12° at lower temperatures (T < 50 °C).
Figure 4
Measurement results for θinit and θsta of DI-water on Teflon AF1600 over temperature.
Measurement results for θinit and θsta of DI-water on Teflon AF1600 over temperature.According to the Young’s equation (eq ) the change of the quasi-static
WCA is governed
by the interface tensions equilibrium: γla·cos
θ = γsa – γsl. As γla stays constant during the evaporation process at a constant
temperature and pressure, the variation of the WCA θinit → θsta is due to the changes of γsa and γsl, consequentlywith Δγs*(θsta, θinit) = γs*sta – γs*init, the subscript s* represents sl and sa. The values of the temperature dependence
of γla is taken from literature[30] and validated by some own experiments. The change of γsa is mainly due to the adsorption of water onto surface, which
can be reduced by temperature. Figure shows that at T = 80 °C the
effective solid surface tension change calculated from experimental
data by γla·(cos θsta –
cos θinit) is ∼3 mN/m. This change can not
be explained by the adsorption of water on a hydrophobic surface at
such high temperature. More details are discussed in the following
soaking experiment part. Besides γla and γsa, the solid–liquid interface tension γsl also contributes to the force equilibrium at the triple-line. The
difference of the solid–liquid tension Δγsl(θsta, θinit) is described
by Gibbs adsorption equation[31]The results for Δγsl(θsta, θinit) are
depicted in Figure with the universal gas constant R, the absolute temperature T, and the molar surface
area of Teflon AF1600 Am (details seen
in Supporting Information). The Δγsl(θsta, θinit) calculated by Gibbs adsorption equation cannot sufficiently
explain the change calculated by Young’s equation from experimental
data γla·(cos θsta –
cos θinit). Consequently, we assume an extra force Ff with static friction-like behavior (see Figure ) to extend the Young’s
equation (eq ) ensuring
the static force equilibriumThe WCAs
are observed over time during the
evaporation process.
Figure 6
Results of effective solid surface tension change γla·Δcos θ from evaporation experiments, the
solid–liquid
interface tension difference Δγsl(θsta, θinit) calculated from Gibbs
adsorption equation, the friction-like force Ff-max evaluated from soaking and evaporation experiments.
All results are plotted against temperatures.
Figure 5
Force equilibrium at the triple-line. Interface tensions
γla, γsl, γsa and
a friction-like
force Ff contribute to the force equilibrium.
Force equilibrium at the triple-line. Interface tensions
γla, γsl, γsa and
a friction-like
force Ff contribute to the force equilibrium.Results of effective solid surface tension change γla·Δcos θ from evaporation experiments, the
solid–liquid
interface tension difference Δγsl(θsta, θinit) calculated from Gibbs
adsorption equation, the friction-like force Ff-max evaluated from soaking and evaporation experiments.
All results are plotted against temperatures.When the droplet is deposited on the solid surface, it adjusts
to an equilibrium shape by the initial interface tensions with an
initial contact radius and an initial WCA θinit: Ffinit = γla ·cos θinit + γslinit – γsainit. The superscript
init refers to the initial solid surface condition (dry) with the
corresponding WCA θinit. By considering the droplet
diameter in this work (∼2 mm, smaller than the capillary length
of water 2.7 mm) and the deposition method, we assume Ffinit = 0.
While the WCA is decreasing, the friction-like force increases up
to its maximum value Ff-max when
the triple-line is depinned and starts moving in CCA mode with the
corresponding θsta. The force equilibrium is then Ff-max = γla·cos
θsta + γslsta – γsasta, where the superscript sta refers
to the solid surface condition in the absorption–desorption
equilibrium state around the triple-line with the corresponding WCA
θsta. Combining the force equilibrium equations,
we havewhere Δγsl(θsta, θinit) can be calculated
by eq with θinit, θsta and the corresponding T.
Contact Angle by Soaking Experiments
From the evaporation
experiments, we know that the triple-line movement for the receding
WCA leads to the direction of the water covered surface, previously
below the droplet. Accordingly, the solid–air interface tension
γsa should have experienced the influence of liquid
water adsorption. The change of γsa can be calculated
based on Gibbs adsorption equation as[16]Δγsa = RT ∫0 Γd ln pv, where Γ is the concentration of adsorbed vapor on a solid
as a function of the vapor pressure pv up to its equilibrium vapor pressure p0 of the liquid. The concentration of adsorbed vapor Γ is hard
to be estimated and also hard to be directed measured in situ for
hydrophobic materials. Consequently, we tried to directly analyze
this effect by another WCA experiment on a sample surface that has
been completely soaked in DI water.First, we immersed the well-cleaned
samples into DI water for 10 min up to 6 h at T =
20, 25, 30 °C allowing the water to adsorb onto Teflon AF1600.
The WCAs on the soaked samples were then measured in the chamber at
the same temperature (see Figure ), while the groove was filled with DI water to ensure
a saturated humidity and therefore prevent the desorption and evaporation.
The immediately following WCA (θsoak) experiments
showed a significant reduction of 4–5° compared to the
initial WCA (see Table. ), while the immersion time had no significant effect on the WCA
reduction. In a second step, we tried to reverse the adsorption process
by heating the sample surface to 50 °C for 10 s and blowing with
nitrogen separately. The followed WCA experiments on those surfaces
again showed the expected large initial WCA.
Table 1
Soaking
Experiment Resultsa
T
θinit
θsoak
θsta
Ff-max
20
121.1 ± 0.01
116.1 ± 0.05
113.3 ± 0.23
2.91 ± 0.13
25
121.0 ± 0.01
117.2 ± 0.03
113.9 ± 0.10
3.36 ± 0.06
30
121.2 ± 0.20
117.7 ± 0.08
114.5 ± 0.09
3.18 ± 0.05
The effective solid energy change
after soaking γla·(cos θsoak – cos θinit) 5.58 mN/m for 20 °C is
comparable with the immersion energy 6 mN/m of Teflon measured by
Chessick et al.[14].
The effective solid energy change
after soaking γla·(cos θsoak – cos θinit) 5.58 mN/m for 20 °C is
comparable with the immersion energy 6 mN/m of Teflon measured by
Chessick et al.[14].On the basis of the results, we conclude that the
physical and
reversible adsorption of water on the Teflon AF1600 surface is a dominating
reason for the WCA reduction at low temperature. With the experimental
results for the θinit on the dry surface and the
θsoak on the soaked surface, we get the WCA change
by using eq where Δγsl(θsoak, θinit) can
be calculated
by eq . Δγsa(θsoak, θinit) = γsasoak – γsainit, equals to Δγsa(θsta, θinit) = γsasta – γsainit with the consideration that the γsasoak and γsasta are both referring
to the solid surface that is covered with water before and in adsorption
equilibrium. With the experimental results of the stabilized WCA θsta, we evaluate eq and eq to
find the force Ff-maxThe
results are listed in Table . The value of Ff-max is
almost constant 3.15 ± 0.19 mN/m,
independent of temperature. The effect of adsorption on the WCA decreases
with temperature and is very limited at temperature higher than 50
°C. The effective solid surface tension change at 80 °C,
γla·(cos θsta – cos
θinit), is mainly due to the friction-like force,
which is consistent with the evaporation experimental result, ∼3
mN/m.
CA Model
From the experimental results, we identified
two contributions
to the force equilibrium at the triple-line: a temperature-independent
friction-like force and a temperature dependent adsorption on solid
surface. The adsorption is hard to measure quantitatively in situ
for hydrophobic materials. We therefore propose a model to describe
the WCA considering the adsorption coverage f on
the solid surface. The adsorption coverage is defined as the area
fraction of the occupied adsorption area to the total adsorption area.[32] The energy contribution of a fully occupied
adsorption area is e with the same unity of γ.
The surface energy for partial adsorption on the solid can be written
aswhere γs0 is the
solid surface
energy in vacuum, originating from the surface relaxation and reconstruction.
It represents the water adsorption-free surface. The interface energy
between the liquid droplet and the solid surface is assumed as γsl = γs0 + e with 100% coverage
(f = 1) based on the fact that the γsl change during evaporation is limited. The solid–air interface
energy for the dry hydrophobic surface is assumed as γsainit = γs0 with 0% coverage (f = 0). When the adsorption–desorption
process reaches its equilibrium, the solid–air interface energy
can be written as γsasta = γs0 + f · e with a equilibrium coverage f. Plugging those conditions into eq , the initial WCA and stabilized WCA are described
byandrespectively. The relation between the initial
WCA and the stabilized WCA is then given byThe friction-like force Ff-max is evaluated from soaking experiments, considered
as temperature independent. e can be calculated from eq . It shows a constant e value in the temperature range from 20 to 50 °C with e = 37.15 ± 0.26 mN/m. The adsorption coverage f over temperature can be therefore calculated with eq . The model shows the
expected low water adsorption ability of Teflon AF1600. The reachable
adsorption coverage at 25 °C is 0.12. This value is comparable
to the earlier results.[13−16] At temperatures higher than 50 °C, the coverage
approaches zero.
Conclusion
In this work, we investigated
the WCA change during evaporation
as a function of temperature and conducted soaking experiments to
explore the influence of adsorption. We evaluated two main contributions
for the WCA variation: a friction-like force, which has a constant
value of 3.15 ± 0.19 mN/m and is temperature independent, and
a contribution of water adsorption on the solid near the triple-line,
which decreases with increasing temperature and completely vanishes
at temperatures higher than 50 °C. Besides these basic findings,
this knowledge is also for application driven developments, such as
the EW-based manipulation of droplets, of high interest. If, for instance,
the triple-line moves to the adsorption-free area by applying voltage
(EW application) or by increasing the droplet volume (establishing
of the advancing CA), the CA variation is dominated by the friction-like
force. If the triple-line moves to the water-absorbed or water-covered
area when turning-off the applied voltage (EW application) or by decreasing
the droplet volume (establishing of the receding CA), the friction-like
force and the contribution of water adsorption are both responsible
for the CA variation and need to be taken into account for a precise
determination of the corresponding CA. Additionally, an increasing
temperature can reduce or completely remove the adsorption-induced
CA variation. Furthermore, we introduced an adsorption relative parameter
coverage f, friction-like force limit Ff-max and propose an adsorption-area density dependent
model to describe the WCA change. Our proposed model is valid for
hydrophobic materials, where discrete adsorption sites are available
and the adsorption does not form continuous films. This simple model
also provides a possibility to estimate the water adsorption coverage
by measuring the WCA change, since the adsorption quantity and coverage
on a hydrophobic thin film is difficult to be directly measured.In further work, the proposed model and the results of WCA at different
temperatures will be carefully expanded for EW-based applications,
thus paving the way for an accurate prediction of droplet manipulation
under different environmental conditions.
Authors: Soraya Terrab; Alexander M Watson; Christopher Roath; Juliet T Gopinath; Victor M Bright Journal: Opt Express Date: 2015-10-05 Impact factor: 3.894
Authors: Patricia B Weisensee; Nitin K Neelakantan; Kenneth S Suslick; Anthony M Jacobi; William P King Journal: J Colloid Interface Sci Date: 2015-05-04 Impact factor: 8.128