Evelyn WANG, et al.
Super-Hydrophobic Copper Oxide
Nanoparticle Copper Oxide is
super-hydrophobic, with greatly increased heat transfer
properties = ++ efficient steam power.
http://www.sciencedaily.com/releases/2013/10/131002103310.htm
Discovery of Charged Droplets Could
Lead to More Efficient Power Plants
Images such as this, showing droplets being shed from a
superhydrophobic surface (light band at center), revealed the
charging of the droplets. (Credit: Nenad Miljkovic and Daniel
Preston)
Oct. 2, 2013 — In a completely unexpected finding, MIT researchers
have discovered that tiny water droplets that form on a
superhydrophobic surface, and then "jump" away from that surface,
carry an electric charge. The finding could lead to more efficient
power plants and a new way of drawing power from the atmosphere,
they say.
The finding is reported in a paper in the journal Nature
Communications written by MIT postdoc Nenad Miljkovic, mechanical
engineering professor Evelyn Wang, and two others.
Miljkovic says this was an extension of previous work by the MIT
team. That work showed that under certain conditions, rather than
simply sliding down and separating from a surface due to gravity,
droplets can actually leap away from it. This occurs when droplets
of water condense onto a metal surface with a specific kind of
superhydrophobic coating and at least two of the droplets
coalesce: They can then spontaneously jump from the surface, as a
result of a release of excess surface energy.
In the new work, "We found that when these droplets jump, through
analysis of high-speed video, we saw that they repel one another
midflight," Miljkovic says. "Previous studies have shown no such
effect. When we first saw that, we were intrigued."
In order to understand the reason for the repulsion between
jumping droplets after they leave the surface, the researchers
performed a series of experiments using a charged electrode. Sure
enough, when the electrode had a positive charge, droplets were
repelled by it as well as by each other; when it had a negative
charge, the droplets were drawn toward it. This established that
the effect was caused by a net positive electrical charge forming
on the droplets as they jumped away from the surface.
The charging process takes place because as droplets form on a
surface, Miljkovic says, they naturally form an electric double
layer -- a layer of paired positive and negative charges -- on
their surfaces. When neighboring drops coalesce, which leads to
their jumping from the surface, that process happens "so fast that
the charge separates," he says. "It leaves a bit of charge on the
droplet, and the rest on the surface."
The initial finding that droplets could jump from a condenser
surface -- a component at the heart of most of the world's
electricity-generating power plants -- provided a mechanism for
enhancing the efficiency of heat transfer on those condensers, and
thus improving power plants' overall efficiency. The new finding
now provides a way of enhancing that efficiency even more: By
applying the appropriate charge to a nearby metal plate, jumping
droplets can be pulled away from the surface, reducing the
likelihood of their being pushed back onto the condenser either by
gravity or by the drag created by the flow of the surrounding
vapor toward the surface, Miljkovic says.
"Now we can use an external electric field to mitigate" any
tendency of the droplets to return to the condenser, "and enhance
the heat transfer," he says.
But the finding also suggests another possible new application,
Miljkovic says: By placing two parallel metal plates out in the
open, with "one surface that has droplets jumping, and another
that collects them … you could generate some power" just from
condensation from the ambient air. All that would be needed is a
way of keeping the condenser surface cool, such as water from a
nearby lake or river. "You just need a cold surface in a moist
environment," he says. "We're working on demonstrating this
concept."
The research team also included graduate student Daniel Preston
and Ryan Enright, who was a postdoc at MIT and the University of
Limerick and is now at Bell Labs Ireland, part of Alcatel-Lucent.
The work received funding from the U.S. Department of Energy
through the MIT Solid-State Solar-Thermal Energy Conversion
Center, the Office of Naval Research and the National Science
Foundation.
Journal Reference:
Nenad Miljkovic, Daniel J. Preston, Ryan Enright, Evelyn N. Wang.
Electrostatic charging of jumping droplets. Nature Communications,
2013; 4 DOI: 10.1038/ncomms3517
http://www.nature.com/ncomms/2013/130927/ncomms3517/full/ncomms3517.html
Nature Communications 4: 2517
doi:10.1038/ncomms3517
27 September 2013
Electrostatic charging of jumping
droplets
Nenad Miljkovic
Daniel J. Preston
Ryan Enright
Evelyn N. Wang
Abstract
With the broad interest in and development of superhydrophobic
surfaces for self-cleaning, condensation heat transfer enhancement
and anti-icing applications, more detailed insights on droplet
interactions on these surfaces have emerged. Specifically, when
two droplets coalesce, they can spontaneously jump away from a
superhydrophobic surface due to the release of excess surface
energy. Here we show that jumping droplets gain a net positive
charge that causes them to repel each other mid-flight. We used
electric fields to quantify the charge on the droplets and
identified the mechanism for the charge accumulation, which is
associated with the formation of the electric double layer at the
droplet–surface interface. The observation of droplet charge
accumulation provides insight into jumping droplet physics as well
as processes involving charged liquid droplets. Furthermore, this
work is a starting point for more advanced approaches for
enhancing jumping droplet surface performance by using external
electric fields to control droplet jumping.
Fig 1
(a) Field emission scanning electron micrograph of a
10-min-oxidized CuO surface.
Fig 2
(a) Schematic showing experimental setup.
Fig 4
High-resolution field emission scanning electron micrographs of
the tested surface
Fig 5
Experimental individual droplet charge (q) as a function of
departing droplet radius (R)
US2013244001
WO2013130955
Superhydrophobic Nanostructures
Inventor(s): WANG EVELYN [US]; ENRIGHT RYAN
[US]; NAM YOUNG SUK [US]; MILJKOVIC NENAD
Applicant(s): MASSACHUSETTS INST TECHNOLOGY
Abstract
Condensation can he an important process in both emerging and
traditional power generation and water desalination technologies.
Superhydrophobic nanostructures can promise enhanced condensation
heat transfer by reducing the characteristic size of departing
droplets via a surface-tension-driven mechanism. A
superhydrophobic surface can include nanostructures of a metal
oxide having further surface modification.
TECHNICAL FIELD
[0003] The present invention relates to superhydrophobic surfaces.
BACKGROUND
[0004] Superhydrophobic surfaces, with static contact angles
greater than 150[deg.], droplet hystereses less than 10[deg.], and
roll-off tilt angles typically less than 2[deg.], resist wetting
and exhibit self-cleaning properties. Such properties are
desirable for coatings on buildings, solar cells, and textiles, as
well as drag reduction and increased heat transfer via drop-wise
condensation. In nature, a wide array of wetland and aquatic plant
leaves exhibit self-cleaning properties and resist wetting upon
the impact of rainfall. Due to the abundance of water, these
wetland plants do not rely on the intake of moisture through their
leaves to hydrate. In fact, their superhydrophobic properties are
a necessity for survival. Shedding water from the surface
dramatically increases the uptake of CO2 for photosynthesis, and
these self-cleaning abilities reduce the formation of bacteria and
fungi that would otherwise thrive in such hot moist climates.
Significant efforts have focused on mimicking the naturally
occurring structures of the lotus leaf, which demonstrates
superhydrophobic self-cleaning properties. However, existing
fabrication methods have limited the ability to accurately mimic
both the surface structures and resulting water-repellent behavior
of the lotus under droplet impact.
SUMMARY
[0005] In general, a superhydrophobic surface can include
nanostructures of a metal oxide having further surface
modification. Superhydrophobic nanostructures can provide enhanced
condensation heat transfer by reducing the characteristic size of
departing droplets via a surface-tension-driven mechanism.
[0006] In one aspect, a superhydrophobic surface can include a
substrate including a metal and including a plurality of
nanostructures on a surface of the substrate including a metal
oxide of the metal, and a surface modifying layer on at least a
portion of the nanostructures.
[0007] In another aspect, a method of making a superhydrophobic
surface can include forming a plurality of nanostructures of a
metal oxide on a substrate of a metal from which the metal oxide
is derived, and depositing a surface modifying layer on at least a
portion of the nanostructures.
[0008] In certain circumstances, metal oxide can be a copper
oxide.
[0009] In certain other embodiments, the surface modifying layer
can include a self-assembled monolayer. The self-assembled
monolayer can be on a metal coating on the nanostructures. The
surface modifying layer includes a thiol on a surface of the
nanostructures. The thiol can be an alkyl thiol, for example, a
fluorinated alkyl thiol. The metal coating can be deposited on the
nanostructures.
[0010] In certain other embodiments, the surface modifying layer
can include a silane on a surface of the nanostructures. For
example, the silane can be an alkyl silane, such as a fluorinated
alkyl silane. The silane can be deposited on the nanostructures.
[0011] In certain other embodiments, the surface modifying layer
can include a fluorinated polymer. The fluorinated polymer can be
deposited on the nanostructures.
[0012] Other features, objects, and advantages will be apparent
from the description and drawings, and from the claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0013] FIGS. 1A-1B represent SEM images and XRD pattern
(FIG. 1C) of copper oxide nanostructures, after 1 min (FIG. 1A)
and 5 min (FIG. 1B-1C) of oxidation. FIG. 1D represents an SEM
image of a cross-section of the nanostructured copper surface
after a 10 minute oxidation step at separate FIB milled spot.
[0014] FIG. 2 represents an image of Cassie behavior of a
macroscopic water droplet placed onto the
Au/thiol-functionalized CuO surface.
[0015] FIG. 3 represents a schematic depiction of the
experimental optical microscopy set-up for analyzing global
condensation behavior.
[0016] FIG. 4A represents an ESEM image capturing the
droplet growth process on the Au/thiol functionalized CuO
surface. FIG. 4B represents a graph showing the droplet apparent
contact angle as a function of the droplet size extracted from
the ESEM data on the Au/thiol functionalized CuO surface.
[0017] FIG. 5A represents a graph showing the droplet
apparent contact angle as a function of the droplet diameter on
the Au/thiol and silane functionalized CuO surfaces. FIG. 5B
represents a schematic depiction showing the predicted evolution
of the droplet shape.
[0018] FIGS. 6A-6D represent ESEM images showing the
emergent droplet morphology on the functionalized CuO surfaces
in the coalescence-dominated growth stage. FIG. 6E represents
time-lapse images of condensation on the silane-coated CuO
surface during ESEM imaging.
[0019] FIGS. 7A-7C represent the nucleation site spatial
distribution. FIG. 7A represents a coordinate map graph showing
the position of the nucleation sites and their nearest neighbor
captured. FIG. 7B represents a graph showing the cumulative
probability distribution of the nucleated droplet nearest
neighbors compared to the predictions for a random distribution.
FIG. 7C represents an OM image capturing the distribution of
droplet nucleation sites on the Au/thiol functionalized CuO
surface.
[0020] FIGS. 8A-8B represent droplet jumping to pinning
transition. FIG. 8A represents a schematic depiction showing the
excess liquid/vapor surface energy. FIG. 8B represents a graph
showing the excess surface energy compared to the work of
adhesion, as a function of the scaled droplet separation
distance.
[0021] FIGS. 9A-9B represent the individual droplet heat
transfer model. FIG. 9A represents a schematic depiction of the
droplet on the condensing surface growing in the
partially-wetting morphology. FIG. 9B represents the droplet
thermal resistance diagram.
[0022] FIGS. 10A-10B represent a series of graphs showing a
model prediction of individual drop growth rates averaged for 12
individual droplets. FIG. 10A represents a graph showing the
experimentally measured droplet diameters as a function of time.
FIG. 10A inset represents a graph showing the model predictions
and a fitted R [alpha] t<1/3 >scaling. FIG. 10B represents
a graph showing the key thermal resistances normalized to the
total thermal resistance corresponding to FIG. 10A as a function
of droplet radius.
[0023] FIG. 11 represents a graph showing a droplet number
density as a function of droplet diameter for steady-state
condensation.
[0024] FIG. 12 represents a graph showing a heat flux ratio
as a function of droplet coalescence length in comparison to a
smooth hydrophobic surface.
[0025] FIGS. 13A-13D represent a series of graphs showing
the overall heat transfer behavior. FIG. 13A represents a graph
showing the predicted overall heat flux as a function of scaled
droplet coalescence length compared to a smooth hydrophobic
surface. FIG. 13A inset represents a graph showing the predicted
heat transfer behavior for three different rp values. FIGS.
13B-13C represent a series of graphs showing the predicted
overall heat flux ratio as a function of droplet coalescence
length with two different [delta]CuO values. FIG. 13D represents
a graph showing the values of qCuO/qF and ¦qCuO/qF¦max for two
different [delta]CuO values.
DETAILED DESCRIPTION
[0026] Condensation is an important process in both emerging and
traditional power generation and water desalination technologies.
Superhydrophobic nanostructures promise enhanced condensation heat
transfer by reducing the characteristic size of departing droplets
via a surface-tension-driven mechanism. See, for example, Boreyko.
J. B. and C.-H. Chen, Self-Propelled Dropwise Condensate on
Superhydrophobic Surfaces. Physical Review Letters, 2009. 103(18):
p. 184501, which is incorporated by reference in its entirety. In
this work, a scalable synthesis technique was investigated to
produce oxide nanostructures on copper surfaces capable of
sustaining superhydrophobic condensation and characterized the
growth and departure behavior of condensed droplets.
Nanostructured copper oxide (CuO) films were formed via chemical
oxidation in an alkaline solution. A dense array of sharp CuO
nanostructures with characteristic heights and widths of 1 [mu]m
and 300 nm, respectively, were formed. A gold film was deposited
on the surface and functionalized with a self-assembled monolayer
to make the surfaces hydrophobic. Condensation on these surfaces
was then characterized using optical microscopy (OM) and
environmental scanning electron microscopy (ESEM) to quantify the
distribution of nucleation sites and elucidate the growth behavior
of individual droplets with a characteristic size of ~1 to 10
[mu]m at low supersaturations. CuO surfaces can offer superior
condensation behavior in terms of emergent droplet morphology and
coalescence dynamics and a significant enhancement in heat
transfer performance when compared to state-of-the-art condensing
surfaces. Furthermore, the chemical-oxidation-based CuO
fabrication process provides a simple and readily scalable method
to create superhydrophobic condensation surfaces that can sustain
droplet jumping behavior. Comparison of the observed behavior to a
recently developed model for condensation on superhydrophobic
surfaces (see, Miljkovic, N., R. Enright, and P. N. Wang, Growth
Dynamics During Dropwise Condensation on Nanostructured
Superhydrophohic Surfaces, in Proceedings of the 3rd
Micro/Nanoscale Heat & Mass Transfer International Conference.
2012, ASME: Atlanta, Ga. and Miljkovic, N., R. Enright, and E. N.
Wang, Dropwise condensation droplet growth dynamics on
superhydrophobic surfaces. unpublished 2011, each of which is
incorporated by reference in its entirety) suggests a restricted
regime of heat transfer enhancement compared to a corresponding
smooth hydrophobic surface due to the large apparent contact
angles demonstrated by the CuO surface.
[0027] Efficient condensation is required for a range of
industrial processes. In particular the efficiency of steam power
cycles, thermal-based desalination, and phase-change-based thermal
management solutions for electronics cooling are functionally
dependent on the condensation behavior of water on heat transfer
surfaces. In the 1930's, Schmidt and co-workers identified
dropwise condensation (DWC) as a superior mode of heat transfer in
comparison to filmwise condensation (FWC) (see Schmidt, E.,
Schurig, W. and Sellschopp, W. Tech. Mech. Thermodynamik, 1, 53-63
(1930), which is incorporated by reference in its entirety).
Subsequent investigations found that DWC heat transfer rates could
be up to an order of magnitude larger than those associated with
FWC. See, for example, Rose, J. W. Proc Instn Mech Engrs, Vol 216,
Part A: J Power and Energy (2002), which is incorporated by
reference in its entirety. To achieve efficient DWC, condensate
droplets must be rapidly removed from the surface because the
increasing droplet size acts as a thermal barrier. DWC is
associated with the periodic departure of large,
thermally-insulating droplets from the surface, typically under
the influence of gravity, that allows for the re-growth of smaller
droplets with reduced thermal resistance on the exposed areas.
Rose and co-workers (id.) have argued that the self-similar
distribution of drop sizes is a significant factor governing the
overall rate of heat transfer. Under the influence of gravity, the
requirement for droplet departure, to first order, is given by
Bo=[rho]gd<2>/[gamma]>=1 where [rho] is the condensate
density, g is the local acceleration due to gravity, d is the
droplet diameter, and [gamma] is the condensate surface tension.
For water, this leads to a distribution of droplets ranging in
size from the critical nucleus (~1 nm) up to the capillary length
(~1 mm). However, recent investigations by Boreyko & Chen
(PRL, 2009) have demonstrated that the upper drop size can be
restricted to less than 100 [mu]m (Bo<10<-3>) via a
surface-tension-driven departure mechanism that occurs on
nanostructured superhydrophobic surfaces. When small droplets
(e.g. ~10-100 [mu]m) merge on suitably designed superhydrophobic
surfaces, they can undergo coalescence-induced droplet ejection or
"jumping" independent of gravity due to the release of excess
surface energy. The nanostructured surface beneath the coalescing
droplets reduces the droplet adhesion to the substrate by
minimizing the solid fraction and breaks the symmetry of the
coalesced droplet. As a result, the droplet accelerates and
departs perpendicular to the surface. Such droplet jumping offers
an avenue to further enhance condensation heat transfer over
conventional dropwise condensation by increasing the time-averaged
density of small droplets, which transfer heat more efficiently
from the vapor to the substrate. Accordingly, these surfaces are
attractive for applications such as atmospheric water harvesting
and dehumidification where the heat fluxes are relatively low and
droplets can be maintained in a highly mobile state.
[0028] In particular, a superhydrophobic surface can be formed
from on a metal substrate by forming a plurality of nanostructures
of a metal oxide on the substrate. The metal oxide can form a
layer on a surface of the substrate. The layer can have a
thickness sufficient to permit acceptable heat transfer through
the layer. The layer can be thin. For example, the metal oxide
layer can be less than 10 micrometers, less than 5 micrometers,
less than 2 micrometers, less than 1 micrometer, less than 0.5
micrometers, or less than 0.1 micrometers in thickness.
[0029] The layer of metal oxide can be grown on the surface in a
manner that produces a variety of surface features, some portion
of which are nanostructures. The layer of metal oxide can be grown
by chemical or electrochemical oxidation of a metal substrate. For
example, a copper substrate can be treated to form a layer of
nanostructured copper oxide on the surface. Alternatively, an
aluminum substrate can be treated to form a layer of
nanostructured aluminum oxide on the surface.
[0030] The nanostructure can have dimensions of approximately 3
[mu]m or smaller, 2 [mu]m or smaller. 1 [mu]m or smaller, or 500
nm or smaller. In certain dimensions, the nanostructure can in
some cases extend to greater dimensions; for example, a
line-shaped feature might be several cm or several mm in length,
or less, e.g., several nm in width up to several urn in length.
Despite the length extending beyond the nanoscale, this feature
would nonetheless be considered a nanostructure, because of the nm
dimension of the width or depth.
[0031] Once the nanostructures have been formed, the surface can
be coated with one or more coating layers. The coating layer can
be selected to impart desired properties on the surface, such as,
for example, mechanical robustness or increased hydrophobicity, or
both. For example, the superhydrophobic surface can include a
surface modifying layer on at least a portion of the
nanostructures. The surface modifying layer can be a single layer
or a multilayer. For example, an initial coating layer, e.g., a
metallic layer can be deposited by (for example) electroless
plating, chemical vapor deposition or atomic layer deposition. The
initial coating layer can be a polymer or a metal. The surface
modifying layer can be a hydrophobic material, such as a polymer
or self-assembled monolayer, directly on the nanostructure or on
the initial coating layer. For example, a silane or a thiol can be
assembled on a surface. The hydrophobic material; e.g., a
hydrophobic polymer, hydrophobic thiol, hydrophobic carboxylic
acid or hydrophobic silane, can include hydrocarbon (e.g., a
saturated hydrocarbon) groups, halohydrocarbon groups (e.g., a
saturated fluorohydrocarbon), or halocarbon groups (e.g., a
perfluorinated alkyl group). In certain examples, the hydrophobic
material can be trichloro(1H,1H,2H,2H-perfluorooctyl)silane,
(tridecafluoro-1,1,2,2-tetrahydrooctyl)-1-trichlorosilane,
(1H,1H,2H,2H-perfluorodecyl acrylate), a Teflon amorphous
fluoropolymer resin, or an alkyl or fluoroalkyl thiol deposited by
appropriate techniques. The hydrophobic material can have C2-C18
groups that can be fluorinated to varying degrees. The
trifluoromethyl or difluoromethyl groups on the surface can allow
the surface properties to be tailored, for example, to have
advancing wetting angles of 105, 110, 115 or 120 degrees,
depending on the choice of fluorinated alkyl group and base
structure.
[0032] For example, the surface modifying layer can be formed on
an oxide nanostructures by gold sputter followed be self-assembly
of a thiol monolayer. However, other more practical techniques,
can be used to make the oxide nanostructures hydrophobic including
initiated chemical vapor deposition of the polymer
poly(1H,1H,2H,2H-perfluorodecyl acrylate) (PFDA), chemical vapor
deposition of a fluorinated silane film (TPFS), dip-coating of a
fluorinated silane film (FDTS), and spin-coating of the polymer
poly(tetrafluoroethylene (PTFE) (w/an adhesion promoter).
[0033] Spin-Coat Functionalization
[0034] A Teflon amorphous fluoropolymer resin (<0.5 wt. %, Du
Pont Polymers, Inc.) can be first dissolved into a FC40 solvent
(3M Inc.). A 1 wt. % fluoroalkyl monosilane solvent (Cvtonix Inc.)
is mixed into the solution to strengthen adhesion between the
hydrophobic layer and copper oxide. The use of fluoroalkyl solvent
can be found to be critical to prevent degradation of
superhydrophobicity. The solution can then be coated on a CuO
nanostructured surface, baked at 180[deg.] C. for 10 min to dry
out the solvent, and then annealed at 340[deg.] C. for >1 hour
to improve the surface uniformity and adhesion. Goniometric
measurements on a smooth surface coated with the Teflon film
typically demonstrate advancing contact angles of [theta]a
120[deg.].
[0035] CVD Functionalization
[0036] A chemical vapour deposition (CVD) process can be used to
attach a conformal self-assembled
trichloro(1H,1H,2H,2H-perfluorooctyl)silane (TPFS) molecular film
to the nanostructured surface. Following a 10 minute O2 plasma
clean, the surface can be exposed to a vapor of PTFS at room
temperature and a pressure of 17.5 kPa (absolute) for a period of
time ranging from 15 minutes to several hours. A strong covalent
bond is formed between the silane molecule and the oxygen group on
the oxide surface via a condensation reaction that produces a HCl
by-product. Following deposition, the sample can be rinsed with a
solvent (such as ethanol) and dried. Following deposition an
optional (not necessary) annealing step can be performed whereby
the substrate is heated to >100[deg.] C. in order to induce
molecular rearrangement producing a more uniform film structure.
Note that the process is not limited to the PTFS molecule, but may
also be performed with silane molecules that contain a similar
ligand allowing for a condensation reaction to occur at the
surface.
[0037] iCVD Functionalization
[0038] Initiated chemical vapour deposition (iCVD), a process
whereby polymerization occurs on the surface to be coated, can be
performed to create a conformal coating of
poly(1H,1H,2H,2H-perfluorodecyl acrylate) (PPFDA) on the CuO
nanostructures. In this process the thickness of the polymer
coating (~10 nm) can be tuned by adjusting the deposition time.
See, for example, Gupta et al. Chem. Mater. 2008, 20 (4), pp
1646-1651. which is incorporated by reference in its entirety.
[0039] Contact angle hysteresis is defined as the difference
between the advancing and receding contact angles, and the
roll-off tilt angle is the angle of a tilted surface at which a
droplet will roll off. These three values are inter-related and
collectively used to determine a surface's ability to demonstrate
self-cleaning behavior. The surface can be superhydrophobic, with
static contact angles greater than 170[deg.], contact angle
hysteresis of less than 2[deg.], and roll-off angles of less than
0.25[deg.]. The surface can also exhibit advantageous condensation
mass and heat-transfer properties.
[0040] The implementation of superhydrophobic surfaces is of
particular interest as a means to improve the efficiency of
thermal and mass transport processes dependent on the condensation
of water. Superhydrophobic condensation can be obtained provided
two criteria are satisfied See Enright, R., et al.,
Superhydrophobic condensation: The role of energy barriers and
size-scale. unpublished, 2011, which is incorporated by reference
in its entirety. The first is an approximately scale-invariant
wetting energy criterion, which determines whether the contact
line remains pinned at the base of a partially wetting droplet,
leading to a weakly-pinned Cassie-like state (see Cassie, A. B. D.
and S. Baxter, Wettability of porous surfaces. Trans. Faraday
Soc., 1944. 40: p. 546, which is incorporated by reference in its
entirety), or de-pins to form a Wenzel droplet. See Quéré, D.,
Wetting and Roughness. Annual Review of Materials Research, 2008.
38(1): p. 71-99. which is incorporated by reference in its
entirety. The pinning energy barrier during growth is given by the
non-equilibrium Wenzel equation, cos [theta]a<W>=r cos
[theta]a, where [theta]a is the advancing contact angle. This
pinning barrier is then compared to the pinning barrier associated
with the droplet advancing over the discontinuous surface in the
Cassie state, cos [theta]a<CB>=-1 (see Choi, W., et al., A
modified Cassie-Baxter relationship to explain contact angle
hysteresis and anisotropy on non-wetting textured surfaces. J.
Colloid Interface Sci., 2009. 339: p. 208-216, which is
incorporated by reference in its entirety), such that a criterion
can be defined to delineate the expected droplet morphology given
by
[0000] [mathematical formula]
[0041] When E*>1 the contact line near the base of the pillars
can overcome the energy barrier to de-pin and a Wenzel drop is
formed. If E*<1 complete de-pinning is prevented and the
droplet spreads over the top of the pillar array forming a Cassie
droplet as the drop size becomes larger than a length scale
characterizing the pinning barrier, R>>1.
[0042] The second criterion for superhydrophobic condensation
introduces a scale requirement by linking a characteristic size of
the roughness defining the pinning energy barrier to the mean
separation distance between nucleation sites (L). For stable
Cassie growth, (L)/l>=2 is the minimum requirement to avoid
by-passing the pinning barrier defined by Eq. 1 during droplet
coalescence.
[0043] In order to apply these surfaces for application in
large-scale heat transfer there is a requirement for scalable
processes compatible with existing engineering heat transfer
materials. Furthermore, the fabrication method should minimize
parasitic resistances that could negate the advantage of this
unique wetting behavior.
[0044] Here a scalable synthesis method is demonstrated for
modifying copper surfaces to create unique oxide nanostructures
that, once functionalized, can maintain Cassie condensation
behavior while minimizing parasitic resistances due to the
self-limiting behavior of the oxidation process. A combination of
imaging and modeling suggests that there is a critical nucleation
density for the CuO surface that delineates heat transfer
enhancement from degradation with respect to a smooth hydrophobic
surface.
[0045] Surface Synthesis & Characterization
[0046] To synthesize the surfaces, commercially available
oxygen-free copper sheet (99.9% purity, 0.8 mm thickness) was cut
into ~1-2 cm<2 >tabs as substrates. Each Cu tab was cleaned
in an ultrasonic bath with acetone for 5 min and rinsed with
de-ionized (DI) water. The substrate was then dipped into a 2.0 M
hydrochloric acid solution for 30 seconds to remove the native
oxide, then triple-rinsed with DI water, and dried with pure
nitrogen.
[0047] Nanostructured copper oxide films were formed by immersing
the cleaned substrate into a hot (~95[deg.] C.) alkaline solution
composed of NaClO2, NaOH, Na3PO4.12H2O, and de-ionized (DI) water
(3,75:5:10:100 wt. %). During the oxidation process, a thin
(<200 nm) Cu2O layer is initially formed on the copper surface
and then re-oxidized to form CuO. FIG. 1A shows that sharp CuO
nanostructures start to grow on the Cu2O intermediate layer. The
surface reaction can be described as (see, Brisard, G. M., et al.,
Application of probe beam deflection to study the electrooxidation
of copper in alkaline media. Electrochimica Acta, 1995. 40(7): p.
859-865, which is incorporated by reference in its entirety):
[0000]
2Cu+2OH<->->Cu2O+H2O+2e<->,
[0000]
Cu2+2OH<->->2Cu2O+H2O+2e<->.
[0048] The height of the oxide nanostructures was approximately 1
[mu]m after 5 minutes of growth (FIG. 1B). After that, the oxide
growth rate significantly slows down to an almost negligible level
as the CuO layer passivates the copper surface. See, Drogowska,
M., L. Brossard, and H. Menard, Influence of anions on the
passivity behavior of copper in alkaline solutions. Surface and
Coatings Technology. 34(4): p. 383-400, which is incorporated by
reference in its entirety. The XRD result (FIG. 1C) shows a strong
CuO peak originating from the sharp oxide nanostructures and a
weak Cu2O peak from the underlying layer. The unique needle-like
morphology of the CuO nanostructures and the self-limiting
behavior of the oxidation process are key minimize parasitic
conduction thermal resistance of the oxide layers (kCuO 0.2
W/m.K).
[0049] To characterize the total oxide thickness of the fabricated
samples, we used focused ion beam milling (FIB) (NVision 40 Dual
Beam Focused Ion Beam, Carl Zeiss GMBH) and SEM imaging. Milling
was performed with normal incidence of the ion beam (sample tilt
of54[deg.]), ion beam energy of 30 keV, and ion current of 300 pA.
The structure cross-sections were obtained by milling 8 [mu]m
deep*20 [mu]m wide trenches. Due to the good milling response of
Cu, surface polishing was not required. All samples were imaged at
36[deg.] tilt using the in lens detector with electron beam
energies of 7 keV. FIG. 1D shows the cross-section images of a
nanostructured sample. The underlying Cu2O oxide thickness was
found to be [delta]Cu2O 300 nm. With the addition of the CuO
nanostructures, the total copper oxide thickness was
[delta]Cu2O+[delta]CuO 1.5 [mu]m. The morphology of the CuO
nanostructures resemble thin, but broad blades converging to a
sharp point with a typical thickness of <=100 nm and average
widths of 300 nm.
[0050] The unique blade-like morphology of the CuO nanostructures,
with a tip dimension of <=10 nm, ensure nucleation within the
structure (as opposed to the tips of the structure) due to the
increased energy barrier associated with nucleation on features
similar in size to the critical nucleation radius (Rc<=35 nm
for water and typical condensation conditions studied here, See,
Kashchiev, D., 2000, Nucleation: Basic Theory with Applications,
Butterworth-Heinemann, Oxford, which is incorporated by reference
in its entirety.). This feature of the nanostructure geometry
promotes the formation of partially-wetting droplet morphologies,
which are essential to minimizing individual droplet thermal
resistance, since Gibb's criterion can be satisfied. See,
Miljkovic, N., Enright, R., and Wang, E. N., 2012, "Effect of
droplet morphology on growth dynamics and heat transfer during
condensation on superhydrophobic nanostructured surfaces," ACS
Nano, 6(2), pp. 1776-1785, Cao, L., Jones, A. K., Sikka, V. K.,
Wu, J. Z., and Gao, D., 2009, "Anti-icing superhydrophobic
coatings," Langmuir. 25(21), pp. 12444-12448, Gibbs, J. W.,
Bumstead, H. A., and Van Name, R. G., 1906, The scientific papers
of J. Willard Gibbs, Longmans, Green and co., New York and Bombay,
and Quéré, D., 2008, "Wetting and Roughness," Annual Review of
Materials Research, 38(1), pp. 71-99, each of which is
incorporated by reference in its entirety. Furthermore, the
self-limiting behavior of the oxidation process is critical to
minimizing the parasitic thermal conduction resistance of the
oxide layers since the bulk thermal conductivities of the two
copper oxide species (kCuO 20 W/m.K, kCu2O 30 W/m.K, see, Kwak,
K., and Kim, C., 2005, "Viscosity and thermal conductivity of
copper oxide nanofluid," Korea-Aust Rheol J. 17(2), pp. 35-40,
which is incorporated by reference in its entirety.) are an order
of magnitude smaller than the native copper substrate (kCuO 400
W/m.K).
[0051] The CuO nanostructures were functionalized by first coating
them with a 30 nm-thick coating of Au followed by the formation of
a self-assembled monolayer (SAM) of
1H,1H,2H,2H-perfluorodecanethiol by immersing the oxidized
substrate in 1 mM ethanol solution for 1 hr. Goniometric
measurements on a smooth thiolated Au surface showed advancing and
receding contact angles of [theta]a=121.1[deg.]+-2.2[deg.] and
[theta]r=106.3[deg.]+-2.4[deg.], respectively, to give a
calculated equilibrium angle of [theta]e=cos<-1>[0.5(cos
[theta]a+cos [theta]r)]=113.5[deg.]+-3[deg.].
[0052] The effective solid fraction of the CuO surface was
extracted from apparent contact angle measurements of a water
droplet placed onto the Au/thiol-functionalized CuO surface,
[theta]<CB>=169.7[deg.]+2[deg.] ([Delta][theta]<=2[deg.])
using the Cassie-Baxter equation, cos [theta]<CB>, yielding
a value of [phi]eff=0.027+-0.011 (FIG. 2). In order to extract the
effective roughness defining the pinning energy barrier in Eq. 1,
contact angle measurements of formamide (Sigma, molecular biology
grade) were performed on both the smooth and nanostructured
surface. The advancing angle on the smooth surface was found to be
[theta]a=95.3[deg.]+-1.4[deg.] ([theta]r=90.2[deg.]+-2.1[deg.]),
while the advancing Wenzel angle on the CuO surface was found to
be [theta]a<W>=160.6[deg.]+-3.2[deg.]
([theta]r<w>=145.9[deg.]+-2[deg.]. Note that the Wenzel
state was inferred by the observation of significant contact angle
hysteresis between the advancing and receding values,
[Delta][theta] 15[deg.]. The measurements yielded reff=10.2+-2.8.
The effective roughness value obtained should be viewed as an
indication of the complex contact line pinning apparent on the
nanostructured CuO rather than a measure of the absolute roughness
defined by the physical area of the rough surface in comparison to
a corresponding smooth surface. See, Blow, M. L., H. Kusumaatmaja,
and J. M. Yeomans, Imbibition through an array of triangular
posts. J. Phys.: Condens. Matter, 2009. 21(464125), which is
incorporated by reference in its entirety.
[0053] OM Condensation Experiments
[0054] Global droplet nucleation and growth behavior was studied
with optical microscopy using a custom built set-up shown
diagrammatically in FIG. 3. A supply of water-saturated N2 was
obtained by sparging a temperature-controlled water reservoir with
dry N2. A reservoir by-pass valve was installed to provide for the
delivery of dry N2 to the sample as it was being cooled to the
test temperature at the beginning of each experiment. The sample
temperature was set using a temperature-controlled stage (Instec,
TS102-00). Good thermal contact between the sample and the
temperature control stage was ensured by interposing a thin layer
of thermal grease (Omegatherm, Omega) with a stated thermal
conductivity of 2.2 W/m.K.
[0055] Once the stage temperature stabilized at the test
temperature, Tw=283+-0.1 K, the by-pass valve was closed to
initiate the flow of water-saturated N2 to the sample enclosure at
a constant flow rate of Q=2.5 l/min, marking the start of the
experiment. The chamber humidity (Hygroclip, Rotronic) was
recorded throughout the experiment. The supersaturation, S=pvpw,
was controlled by adjusting the water reservoir temperature
through which the N2 was sparged. Droplet nucleation and growth
was recorded at intervals of 0.1 seconds using a high-speed (CMOS)
camera (Phantom v7.1, Vision Research), operating at a resolution
of 800*600 and having a physical pixel size of 22 [mu]m, attached
to an upright microscope (Eclipse LV100, Nikon). Imaging was
performed with either a 40* (Plan Fluor ELWD, Nikon) or a 100* (L
Plan SLWD, Nikon) objective. The relationship between length and
pixel count was calibrated with the known pillar spacing of
microstructured surface previously found using scanning electron
microscopy.
[0056] ESEM Condensation Experiments
[0057] The details of the nucleation and growth of condensed
droplets on the functionalized CuO surface were studied using an
environmental scanning electron microscope (Zeiss EVO 55 ESEM).
Back scatter detection mode was employed with a high gain. The
water vapor pressure in the ESEM chamber was 1.55 kPa. Typical
image capture was obtained with a beam potential of 20 kV and
variable probe current depending on stage inclination angle. A 500
[mu]m lower aperture was used in series with a 1000 [mu]m variable
pressure upper aperture for greater detail. The sample temperature
was initially set to 285+-0.1 K using a cold stage and allowed to
equilibrate for 5 minutes. After equilibration, the surface
temperature was decreased to 284+-0.1 K resulting in nucleation of
water droplets on the sample surface due to condensation of the
saturated water vapour.
[0058] Images and recordings were obtained at an inclination angle
of 70[deg.] to 80[deg.] from the horizontal; at a working distance
ranging from 3 to 5 mm. This was done to ensure good imaging of
the droplet nucleation dynamics at the surface, not typically seen
with an overhead nucleation image, and to minimize substrate
heating due to the electron beam. Recordings were performed at a
500 ms frame speed corresponding to two frames per second. To
ensure good thermal contact between the sample and cold stage,
copper tape was used for mounting.
[0059] Geometric Evolution of Individual Droplets
[0060] The droplet growth behavior on the hydrophobic CuO surfaces
(FIG. 4A) was characteristic of the Cassie wetting state emerging
from a pinned wetted region on the surface consistent with an
estimated E*(reff) 0.19. The ESEM images of water droplets showed
strong topographic contrast such that reliable contact angle
measurements could be made. See, Donald, A. M., et al.,
Topographic contrast of partially wetting water droplets in
environmental scanning electron microscopy. Journal of
Microscopy-Oxford, 2001. 204: p. 172-183, which is incorporated by
reference in its entirety. Droplet contact angles were determined
by fitting a circle to each individual droplet (spherical
approximation) and determining the slope of the tangent where the
droplet neck intersects the fitted circle. This was more difficult
for larger droplets due to the difficulty in determining where the
base of the droplet intersects the fitted circle, resulting in a
larger error and fewer data points. Each contact angle measurement
was recorded along with the droplet diameter (FIG. 4B). The error
associated with the droplet diameter measurement was due to the
image resolution. The CuO droplet morphology showed an initially
varying contact angle (R<=3 [mu]m) due to local pinning of the
droplet contact line until the advancing angle is reached R 3
[mu]m, whose value is consistent with the macroscopically measured
value (FIG. 2). The effective diameter of the pinned region can be
estimated to be ~1-2 [mu]m based on the early stage contact angle
behavior, which is consistent with the characteristic spacing of
the CuO nanostructures estimated as l~[square root of]{square root
over ([pi])}d/2[square root of]{square root over
([sigma]eff)}=1.63 [mu]m. This pinning behavior is in agreement
with previous studies of droplet growth on well-controlled
nanopillars geometries and Cu(OH)2 nanowires. See, Rykaczewski, K.
and J. H. J. Scott, Methodology for imaging nano-to-microscale
water condensation dynamics on complex nanostructures. ACS Nano,
2011. 5(7): p. 5962-5968, which is incorporated by reference in
its entirety.
[0061] In FIG. 5A, the apparent contact angle behavior of
condensed droplets growing on the hydrophobic CuO in surfaces at
S=1.07+-0.1 during ESEM imaging is shown. The ESEM images of water
droplets showed strong topographic contrast allowing reliable
contact angle measurements to be made. See, Donald, A. M.,
Stelmashenko, N. A., Craven, J. P., Terentjev, E. M., and Thiel,
B. L., 2001, "Topographic contrast of partially wetting water
droplets in environmental scanning electron microscopy." Journal
of Microscopy-Oxford, 204(2), pp. 172-183, which is incorporated
by reference in its entirety. Droplet contact angles were
determined by fitting a circle to each individual droplet
(spherical approximation) and determining the droplet radius R and
the height of the spherical segment H. The contact angle was
calculated from R and Has
[0000] [mathematical formula]
[0062] This image processing was more difficult for lower viewing
angles (i.e. larger droplets) due to the challenge in determining
where the base of the droplet intersects the fitted circle,
resulting in a larger error and fewer data points. The error
associated with the droplet radius measurement was due to the
limit of the image resolution (typically 200-500 nm). The CuO
droplet morphology showed an initially varying contact angle
(R<=3-4 [mu]m) because of locally pinned contact lines at the
droplet base. Radius-dependent contact angle behavior continued up
to the point where the interface of the droplet made contact with
surrounding nanostructures and began spreading over the surface in
the Cassie state with an approximately constant advancing angle.
The observed advancing angle compares reasonably well with the
macroscopically measured value of [theta]a<CB> 165[deg.].
The early stage variation in the apparent contact angle was
modeled as
[0000] [mathematical formula]
[0000] assuming a fixed pinned base area of Ap [pi]rp<2
>underneath the individual droplets before coalescence (FIG.
5B). In FIG. 5A, the apparent contact angle of droplets as a
function of the droplet diameter extracted from the ESEM data on
the Au/thiol (red circles) and silane (blue squares)
functionalized CuO surfaces (pv=1300+-75 Pa, Tw=283+-1.5 K,
S=1.07+-0.1) was plotted. The solid curve is defined as
[theta]app=cos<-1>(rp/R)+90[deg.] with rp=1.5 [mu]m. The
dashed dot curves represent the bounds of Eq. 3 for rp=1.5+-0.5
[mu]m. The horizontal dashed line represents the macroscopically
measured apparent contact angle, [theta]app 165[deg.]. The inset
shows a typical ESEM image captured during the droplet growth
process on the silane functionalized CuO surface. FIG. 5B shows
the evolution of the droplet shape predicted by Eq. 3 for
90[deg.]<=[theta]app<=170[deg.] in steps of 20[deg.]
(droplets bounded by solid curves). The model fit (dashed lines)
is defined as [theta]CuO(R)=40[deg.]+43.32R[deg.] (R<=3 [mu]m)
and [theta]CuO=170[deg.] (R>3 [mu]m). Fitting Eq. 3 to the
extracted contact angle data, we estimated that the characteristic
radius of the pinned region to be rp 1-2 [mu]m, which compares
well with the characteristic spacing of the CuO nanostructures
estimated as l=[square root of]{square root over
([pi])}d/(2[square root of]{square root over ([sigma]eff)})=1.2 82
m with d=300 nm and [sigma]eff =0.05. This pinning behavior is in
agreement with previous studies of droplet growth on
well-controlled nanopillars geometries and Cu(OH)2 nanowires. See,
Enright, R., Miljkovic, N., Al-Obeidi, A., Thompson, C. V., and
Wang, E. N., 2012, "Condensation on superhydrophobic surfaces: The
role of local energy barriers and structure length scale,"
Langmuir, 28(40), pp. 14424-14432, and Rykaczewski, K. and J. H.
J. Scott, Methodology for imaging nano-to-microscale water
condensation dynamics on complex nanostructures. ACS Nano, 2011.
5(7): p. 5962-5968, each of which is incorporated by reference in
its entirety.
[0063] Emergent Droplet Morphology
[0064] The influence of the nucleation density on the emergent
wetting state was explored using optical microscopy. Optical
microscopy offers an advantage over ESEM since larger vapor
pressures can be achieved without compromising image quality.
Partially-wetting Cassie behavior with jumping droplets emerged on
the Au/thiolated CuO surface where (L)=0.5N<-0.5> 8.1 [mu]m
obtained by focusing at the surface (top, FIG. 6A) and confirmed
by focusing through the droplets (below, FIG. 6B) to show the
wetting state. In FIGS. 6A-6B, condensation on the Au/thiolated
surface at S 1.5 resulted in a nucleation density of N=4*10<9
>m<-2>. The red arrow in the inset of FIG. 6B points to a
light-absorbing region surrounded by a light-reflecting region
indicative of the partial-wetting morphology (Inset scale bar: 10
[mu]m). The droplets were found to be weakly pinned to the surface
as evidenced by the observation of droplet jumping (coalescing
droplets disappeared from the field of view). Focusing through the
droplets (FIG. 6B) revealed that, in most cases, a single dark
light absorbing region surrounded by a bright reflective ring was
located beneath each droplet indicative of a partially-wetting
Cassie state. The approximate sizes of the pinned base of the
droplets were found by fitting circles to the dark regions. The
magnification factor due to focusing through the nominally
spherical droplets was estimated from M=n/(2-n) 2 (see, Wang, Z.,
Guo, W., Li, L., Luk'yanchuk, B., Khan, A., Liu, Z., Chen, Z., and
Hong, M., 2010, "Optical virtual imaging at 50 nm lateral
resolution with a white-light nanoscope," Nature Communications,
2, 218, which is incorporated by reference in its entirety), where
a refractive index of n=1.33 was used for water. Image processing
of the measurements gave rp=1.09+-0.13 [mu]m consistent with the
contact angle behavior observed in FIG. 5.
[0065] In contrast, condensation on the silanated surface at S 1.5
(FIG. 6C-6D) resulted in a nucleation density of N>5*10<10
>m<-2 >despite the fact that both the thiol and silane
molecules are CF3 terminated (i.e., same nominal surface energy).
Mixed-mode wetting behavior with pinned droplets on the silanated
CuO surface where (L)=0.5N<-0.5><2.2 [mu]m obtained by
focusing at the surface (top, FIG. 6C) and confirmed by focusing
through the droplets (below, FIG. 6D) to show the wetting state.
This large nucleation density led to the formation of highly
pinned droplets that developed irregular shapes following
coalescence events (i.e., no coalescence-induced jumping
observed). This behavior was in contrast to that observed at lower
supersaturations in the ESEM where droplet jumping was observed on
the silanated CuO surface, FIG. 6E shows time-lapse images of
condensation on the silane-coated CuO surface during ESEM imaging.
The dashed and solid circles indicate droplet groups before and
after coalescence, respectively (ESEM conditions: pv=800+-75 Pa
and Tw=276+-1.5 K (S=1.07+-0.1)). Focusing through the droplets
(FIG. 5D) showed a number of light absorbing and reflecting
regions under the larger droplets formed by coalescence events
consistent with a mixed mode wetting state rather than complete
wetting. See, Wier, K. A., and Mccarthy, T. J., 2006,
"Condensation on ultrahydrophobic surfaces and its effect on
droplet mobility: ultrahydrophobic surfaces are not always water
repellant," Langmuir, 22(6), pp. 2433-2436, which is incorporated
by reference in its entirety.
[0066] Distribution of Nucleation Sites
[0067] To understand emergent morphology on the functionalized CuO
surfaces in the coalescence-dominated growth stage, we first
investigated the distribution of nucleation sites on the
Au/thiol-functionalized surface. FIG. 7A shows a coordinate map
showing the position of the nucleation sites (blue dots) and
arrows indicating their nearest neighbor captured using optical
microscopy at 100* magnification on the Au/thiol functionalized
CuO surface at t=10 s after the start of the experiment (S 1.5,
N=3.83*109 m<-2>) (FIG. 6A-6B). FIG. 7B shows the cumulative
probability distribution of the nucleated droplet nearest
neighbors (red circles) compared to the predictions for a random
distribution, P=1-e<-N[pi]L><<2 >>(solid line).
The mean separation distance between nucleation sites is given by
2L[square root of]N=1. The horizontal bars represent the bin
width. FIG. 7C shows an OM image capturing the distribution of
droplet nucleation sites (S 1.5, N=4*10<9 >m<-2>) on
the Au/thiol functionalized CuO surface at t=10 s after the start
of the experiment. The distribution of nucleation sites from FIG.
7C were analyzed and found to be in good agreement with the
Poisson distribution indicating a spatially random nucleation
process such that the mean nearest neighbor is given by:
[0000]
L0.5N<-0.5 > (4)
[0068] See, Gaertner, R. D., Distribution of active sites in the
nucleate boiling of liquids. Chem. Eng. Prog., 1963. 59: p. 52-61,
which is incorporation by reference in its entirety.
[0069] However, the observation of nucleation at low
supersaturations, S<=1.5, is inconsistent with kinetic
nucleation theory, which predicts a critical supersaturation
Sc>2.5 for water condensing on hydrophobic surfaces
([theta]>90[deg.]). See, Kashchiev, D., Nucleation: Basic
Theory with Applications. 1 ed. 2000, Oxford:
Butterworth-Heinemann., which is incorporated by reference in its
entirety. This seeming inconsistency has been linked to
randomly-distributed defects in the molecular film coatings used
to impart hydrophobicity, which expose the underlying
(highly-wettable) substrate creating active nucleation sites. See,
Enright, R., et al., Superhydrophobic condensation: The role of
energy harriers and size-scale. unpublished, 2011, which is
incorporated by reference in its entirety. Thus, we attribute the
distinctly different condensation behavior observed in FIG. 6 to
the defect density associated with the two functionalization
methods and the resulting discrepancy in the number of active
nucleation sites at S 1.5.
[0070] Droplet Jumping to Pinning Transition
[0071] The transition to a non-jumping mixed-mode wetting state
regime can be understood by considering that, as the spacing
between nucleation sites L approaches the length scale of the
partially-pinned region under a droplet rp, the excess surface
energy released during coalescence due to a change in liquid/vapor
interfacial area [Delta]A at constant volume V is unable to
overcome the constant work of adhesion associated with the pinned
region under the coalescing droplets. Assuming that complete
de-wetting of the liquid from the structured region is
energetically unfavorable compared to some portion of the liquid
remaining pinned within the structures on the surface, the work of
adhesion required to create new interfacial area is
W1/[gamma]Ap=[(2-[sigma])+[sigma] cos [theta][gamma]] 2 (for
[sigma]->0). To calculate the excess surface energy
[Delta]E([sigma]app, R) available for droplet jumping we
considered the situation shown in FIG. 8A. Two droplets of equal
diameter coalesce resulting in the formation of a single jumping
droplet. Considering only the volume of liquid not pinned within
the structure, the energy balance between states 1 and 2 is given
by
[0000]
[Delta]E=E2-E1=[gamma][pi][4R<2>(cos
[theta]app(R)-1)-4<1/3><2/3>(R<3>(3+cos
[theta]app(R))(cos [theta]app(R)-1)<2>)<2/3>], (5)
[0000] where cos [theta]app(R) is obtained from Eq. 3. The total
work of adhesion W was estimated based on the partially-wetted
area under each droplet Ap. Neglecting the functionalized CuO
contribution to w1 since [sigma] 0, the work of adhesion for two
droplets is then
[0000]
w=2W1=4[gamma]Ap. (6)
[0072] When the magnitudes of [Delta]E and W are comparable or
when W dominates (¦[Delta]E/W¦<=1), there is little or no
energy available in the system of the two droplets to power
jumping. Thus, upon coalescence the newly formed droplet remains
on the surface with either one or two wetted regions in the
apparent base area, while the remainder of the apparent base area
resides in the Cassie state (mixed mode wetting state). However,
when ¦[Delta]E/W¦>>1, sufficient excess surface energy is
available for conversion into the kinetic energy for droplet
jumping, provided that other dissipation mechanism do not play a
significant role. See, Boreyko, J. B., and Chen, C.-H., 2009,
"Self-propelled dropwise condensate on superhydrophobic surfaces,"
Phys. Rev. Lett., 103(18), pp. 184501, which is incorporated by
reference in its entirety.
[0073] In FIG. 8A, the excess liquid/vapor surface energy was
estimated by considering the difference in energy between states
E1 and E2. Energy is required to overcome the work of adhesion to
form a liquid/vapor interface of area 2Ap for the two pinned necks
of the coalescing droplets. In FIG. 8B, ¦[Delta]E/W¦ is plotted as
a function of the droplet coalescence length, L=2R, scaled by the
characteristic diameter of the pinned region beneath the droplet,
2rp, according to to Eqs. 5 and 6. Three values of rp (=1 [mu]m,
1.5 [mu]m and 2 [mu]m) are shown for each surface. Increasing rp
results in smaller values of ¦[Delta]E/W¦. We observe that
¦[Delta]E/W¦~[L/(2rp)]<2>. For rp=1 [mu]m, the model
predicts ¦[Delta]E/W¦=0.07 (no jumping) and ¦[Delta]E/W¦=6.27
(jumping possible) for the silanated CuO ((L)/(2rp)=1.1, blue
squares) and thiolated CuO (L/(2rp)=4.05, red circles),
respectively, consistent with the observed behavior in FIG. 6. The
shaded region ((L/(2rp)<=1) marks the transition to the Wenzel
state. The horizontal bars for each point show +-[square root
of]{square root over ((L))}. The large spread in separation
distances indicates the possibility of a mixed behavior of droplet
jumping and pinning on the same surface. Increasing rp from 1
[mu]m to 2 [mu]m reduces ¦[Delta]E/W¦ to 1.1 for the Au/thiol
surface. For the silane surface, the same increase in rp results
in (L)/(2rp)<1. Based on the observed jumping behavior of the
Au/thiol surface and the mixed modes observed on the silane
surface, we conclude that the pinned radius is in the range of 1
[mu]m<=rp<=1.5 [mu]m, which is consistent with our optical
measurements of the pinned base region.
[0074] Individual Droplet Heat Transfer Model
[0075] To quantify the heat transfer behavior of individual
droplets growing on the nanostructured CuO surface, we used a
steady-state heat transfer model that captures the key thermal
resistances from the saturated vapor atmosphere in the ESEM to the
condensing structured surface for heat transferring through a
single droplet. See. Miljkovic et al. (ACS Nano, 2012) and
Miljkovic, N., Enright, R., and Wang, E. N., 2012, "Growth
dynamics during dropwise condensation on nanostructured
superhydrophobic surfaces," Proceedings of the 3rd Micro/Nanoscale
Heat & Mass Transfer International Conference, Atlanta, Ga.,
USA, March 3-6, each of which is incorporated by reference in its
entirety.
[0076] The geometry and thermal resistance network defined in the
model in shown in FIG. 9. FIG. 9A shows a schematic diagram of the
droplet on the condensing surface growing in the partially-wetting
morphology. FIG. 9B shows a droplet them<->Jai resistance
diagram showing the droplet curvature ([psi]c), liquid-vapor
interface ([psi]i), droplet conduction ([psi]d), hydrophobic
coating ([psi]hc), CuO nanostructure ([psi]CuO), liquid bridge
([psi]w) and Cu2O under layer ([psi]Cu2O) thermal resistances.
[0077] The first resistances encountered as heat is transferred
from the saturated vapor to the substrate are those associated
with the droplet curvature ([psi]c) and liquid-vapor interface
([psi]i), which govern the kinetics of the phase change process.
The depression of the saturation temperature due to the interface
curvature leads to a thermal resistance given by,
[0000] [mathematical formula]
[0000] where q is the total heat transfer rate through the
droplet, [gamma] is the surface tension, Rc is the critical nuclei
radius, TS is the depressed saturation temperature of the vapor
near the liquid/vapor interface, hfg, is the latent heat and
[rho]w is the liquid density. See, Carey, V. P., 2008,
Liquid-Vapor Phase-Change Phenomena, Taylor & Francis Group,
LLC, New York & Oxen, which is incorporated by reference in
its entirety.
[0078] The thermal resistance between the curvature-depressed
saturated vapor and the liquid at the liquid-vapor interface is
given by
[0000]
[psi]i=[h, 2[pi]R<2>(1-cos [theta]app)]<-1 > (8)
[0079] The condensation interfacial heat transfer coefficient hi
is given by
[0000] [mathematical formula]
[0000] where R=461.5 J/kg.K and [nu]1v, are the specific gas
constant and the change in specific volume between the vapor and
liquid phases of water, respectively. See, Choi, W., Tuteja, A.,
Mabry, J. M Cohen, R. E., and Mckinley, G. H., 2009, "A modified
Cassie-Baxter relationship to explain contact angle hysteresis and
anisotropy on non-wetting textured surfaces," J. Colloid Interface
Sci., 339(1), pp. 208-216, which is incorporated by reference in
its entirety.
[0080] The locally reduced saturation temperature is given by
TS=Tsat-[psi]cq. The condensation coefficient, a, is the ratio of
vapor molecules that will be captured by the liquid phase to the
total number of vapor molecules reaching the liquid surface
(ranging from 0 to 1). We assumed [alpha]=0.9, which is
appropriate for clean environments such as the ESEM (See, Carey,
V. P., 2008, Liquid-Vapor Phase-Change Phenomena, Taylor &
Francis Group, LLC, New York & Oxen, which is incorporated by
reference in its entirety.), but in fact the model results were
not sensitive to the condensation coefficient ranging from 0.5 to
1 in this study. Eq. 9 is strictly valid for
(qt<11>[nu][nu]/hl[nu])(2*RTS)<1/2><<1, where
qt<11>/hl[nu] is the mass flux crossing the liquid/vapor
interface. For the range of calculations performed here we found
that the maximum (qt<11>[nu][nu]/hl[nu])(2*RTS)<1/2>
1*10<-12>. The latent heat released during phase change is
then conducted through the droplet having a thermal resistance
([psi]d) that varies with [theta]app(R) (FIG. 5) given by Kim, S.,
and Kim, K. J., 2011, "Dropwise condensation modeling suitable for
superhydrophobic surfaces" J. Heat Transfer, 133(8), pp.
081502-1-081502-7, which is incorporated by reference in its
entirety.
[0000] [mathematical formula]
[0081] Heat is then conducted from the apparent base of the
droplet through the nanostructured region to the substrate through
thermal resistances due to the hydrophobic coating ([psi]hc), the
nanostructures ([psi]CuO), the area of pinned liquid underneath
the droplet ([psi]w), and the underlying oxide ([psi]Cu2O). By
approximating this composite region as a parallel heat transfer
pathway from the apparent base of the droplet to the substrate
surface we obtain
[0000] [mathematical formula]
[0082] where kw is the thermal conductivity of water, khc is the
thermal conductivity of the functional coating ( 0.2 W/m.K for a
molecular monolayer) and [delta]hc is the functional coating
thickness ( 1 nm). Finally, the thermal resistance of the Cu2O
layer is given by
[0000] [mathematical formula]
[0083] After summing Eqs. 7, 8, 10, 12 and rearranging, the heat
transfer rate is
[0000] [mathematical formula]
[0084] where [Delta]T is the temperature difference between the
saturated vapor and the substrate temperature underneath the Cu2O
layer. The droplet heat transfer rate is then related to the
droplet growth rate dR/dt by
[0000] [mathematical formula]
[0085] In this formulation, the apparent contact angle can be
defined as a function of the drop radius as given by Eq. 3. See,
Miljkovic, N., Enright, R., and Wang, E. N., 2012, "Modeling and
optimization of condensation heat transfer on micro and
nanostructured superhydrophobic surfaces," J. Heat Transfer,
accepted, which is incorporated by reference in its entirety.
[0086] Equating Eqs. 13 and 14, an expression for the droplet
growth rate is obtained that is solved numerically to determine
the droplet radius as a function of time. See, Miljkovic et al.
(ACS Nano, 2012). To obtain sufficient accuracy and resolution,
the time step used in the numerical simulation was [Delta]t=0.01
s. Material properties were obtained using NIST software (REFPROP)
such that all input parameters used were temperature dependent.
See, Lemmon, E. W., Mclinden, M. O., and Friend, D. G., 2005, NIST
Chemistry WebBook, NIST Standard Reference Database Number 69,
National Institute of Standards and Technology, Thermophysical
properties of fluid systems, which is incorporated by reference in
its entirety.
[0087] Model Prediction of Individual Drop Growth Rates
[0088] In FIG. 10A, the measured droplet radii as a function of
time for 12 individual droplets were compared to the predictions
of the heat transfer model described above. The experimentally
measured droplet diameters as a function of time (red circles) are
compared to the individual droplet growth model (solid curve) with
rp=1.5 [mu]m, [delta]CuO=1.5 [mu]m (ESEM conditions: pv=800+-75 Pa
and Tw=276+-1.5 K (S=1.07+-0.1)). The inset shows the experimental
data, the model predictions and a fitted R[proportional
to]t<1/3 >scaling (dashed curve) in log coordinates. The
error bars correspond to uncertainty in the measured droplet
radius. The data was best fit by [Delta]T=0.034 K, which is within
the uncertainty of the measurements of temperature and pressure in
the ESEM chamber. This value was chosen based on the best fit
between the model and experimental growth rate data. The results
of the observed behavior compare well to the classic power law
growth model for condensation. See, Fritter, D., Knobler, C. M.,
and Beysens, D. A., 1991, "Experiments and simulations of the
growth of droplets on a surface (breath figures)," Phys. Rev. A,
43(6), pp. 2858-2869, which is incorporated by reference in its
entirety.
[0089] When droplet dimensions are larger than the pinned region
(R>2 [mu]m), we expect the droplet radius to follow a power law
over time R=At<b>, where A is a constant, t is time and b,
the power law exponent, ranges from 0 to 1 depending on the
substrate dimensionality and growth limiting mechanism. During
initial growth without coalescence (R<4 [mu]m), the power law
exponent of b=[3/4] could be reasonably fitted to the data. This
value was within the range of 0 to 1, but differs from b=[1/3]
expected for diffusion limited growth. This result indicates that
a diffusion process was not the major limiting growth mechanism.
However, at long times the b=[1/3] growth exponent was recovered,
coinciding with diffusion limited growth due to conduction through
the droplet bulk.
[0090] FIG. 10B gives a breakdown of the component thermal
resistances normalized to the total thermal resistance predicted
by the model during droplet growth. The vertical line delineates
the transition from radius-dependant apparent contact angle
([theta]app(R)) to a fixed contact angle equal to the
macroscopically measured apparent advancing contact angle
([theta]a<CB>) at 2R=11 [mu]m.
[0091] The model predicts that at small droplet radii (R<=3
[mu]m), growth rates were limited by the combination of the
conduction resistance of the droplet volume pinned within the
nanostructures
((([psi]hc+[psi]CuO)<-1>+([psi]w+[psi]hc)<-1>)<-1>)
and the interface curvature resistance ([psi]c) that effectively
reduces the driving pressure difference for vapor molecules
attaching to the liquid-vapor interface. The interfacial
resistance (p) was found to contribute little to the total
resistance, peaking at [psi]i/[psi]T=0.17 for R=0.95 [mu]m before
dropping off to [psi]i/[psi]T<0.01 at larger radii. Similarly,
the Cu2O layer ([psi]Cu2O) beneath the CuO nanostructures also
contributed negligibly to the total thermal resistance,
[psi]Cu2O/[psi]T 0.02. Beyond R>8 [mu]m, the heat transfer
process was increasingly limited by the conduction resistance
within the droplet bulk. See, Miljkovic et al. (ACS Nano, 2012).
[0092] Droplet Number Density as a Function of Droplet Diameter
[0093] To discern the mean coalescence length for condensed
droplets on the CuO nanostructure, the droplet size distribution
was measured from the ESEM images. Droplet number density and size
were measured from multiple images of the steady-state
condensation process over several cycles of droplet growth,
coalescence-induced jumping and re-growth for ESEM conditions:
pv=800+-75 Pa, Tw=276+-1.5 K, S=1.07+-0.1 (ImageJ and Adobe
Photoshop), accounting for inclination angle and total frame size
(FIG. 11). The counting error associated with the droplet number
density was estimated to be ~10% at each size range.
[0094] Due to a nucleation density of N 1*10<10
>m<-2>, the mean center-to-center spacing of the droplets
was 5 [mu]m and coalescence-induced jumping (see, Boreyko, J. B.
and C.-H. Chen, Self-Propelled Dropwise Condensate on
Superhydrophobic Surfaces. Physical Review Letters, 2009. 103(18):
p. 184501, which is incorporated by reference in its entirety)
maintained a majority portion of the droplet distribution below 10
[mu]m as shown in FIG. 11.
[0095] Heat Transfer Performance of the CuO Surface
[0096] To predict the heat transfer performance of the CuO
surface, the observed growth behavior was incorporated into a
recently developed model. The steady state condensation heat flux
was first estimated by modeling the heat transfer rate through an
individual drop. Heat is transferred from the saturated vapor to
the liquid-vapor interface through resistances associated with
droplet curvature (rc) and liquid-vapor interface (ri). The heat
is conducted through the droplet and the nanostructures to the
substrate through thermal resistances due to conduction through
the droplet that incorporates the contact angle behavior as a
function of droplet size (FIG. 4) (rd), the hydrophobic coating
(rhc), the nanostructures and underlying oxide (rn) and the area
of pinned liquid underneath the droplet (rg). The single drop
behavior was then multiplied by the droplet size distribution and
integrated over all radii given by:
[0000]
q<n>=[integral]R*<R><eff
>q(R)n(R)dR+[integral]Reff<R><max >q(R)N(R)dR. (15)
[0097] Eq. 15 was used to compare the heat flux performance for
the CuO surface to a corresponding smooth thiolated surface with a
contact angle corresponding to the advancing angle
([theta]a=120[deg.]). The droplet coalescence length L was set
equal to the effective radius Reff and varied by changing
nucleation density according to Eq. 4. To make a conservative
comparison of performance, the nucleation density for both
surfaces was assumed to be equal. For the flat surface a fixed
departure size, R=2 mm, was assumed. The departure size for the
CuO surface was equated to L assuming ideal coalescence-induced
jumping behavior, i.e., inviscid limit with no influence of
variable contact angle. FIG. 12 demonstrates that, for L>5
[mu]m, the CuO surface degrades heat transfer performance in
comparison to the smooth surface. A 2* peak is observed at L 2
[mu]m, but performance drops for smaller L as the curvature
resistance begins to play a significant role. However, for the CB
state to arise it is necessary to remain above the critical L/l,
which limits the maximum enhancement to ~1.6* at L 3 [mu]m.
[0098] The predicted behavior can be explained in terms of the key
thermal resistances. During early stages of growth (R<=6
[mu]m), the conduction resistance (rd) through the droplet is
negligible compared to the other thermal resistances. Therefore,
for a droplet on the CuO surface, the nanostructure (rn+rhc) and
liquid bridge (rg+rhc) resistances are dominant. However, for
R>=6 [mu]m the performance is limited by the large apparent
contact angle of droplets on the CuO surface, which causes
significant thermal resistance due to the limited droplet basal
contact area. This can be seen in FIG. 12 where the effect of
reducing the nanostructure height was explored while assuming
identical contact angle behavior. The peak enhancement is observed
to increase to ~3.5* (or ~2.75* to remain above the critical L/l
ratio), but the maximum "break-even" coalescence length does not
change to a great extent, increasing from ~5 [mu]m to ~7 [mu]m.
[0099] Overall Heat Transfer Behavior
[0100] To estimate the overall heat transfer performance of the
nanostructured CuO surface, the individual droplet growth behavior
was incorporated into an expression for the droplet size
distribution and integrating over all radii given by)
[0000]
Q''=[integral]Rc<(L)/2
>q(R)n(R)dR+[integral](L)/2<R><maN>q(R)N(R)dR. (16)
[0000] where q'' is the overall steady-state condensation heat
transfer rate per unit area of the condensing surface, (L)/2 is
the mean droplet coalescence radius, q(R) is the individual
droplet heat transfer (Eq. 14), n(R) is the non-interacting
droplet size distribution, N(R) is the coalescence dominated
droplet size distribution and Rmax is the droplet departure size.
The first integral in Eq. 16 primarily captures the heat flux due
to individual droplet growth before coalescence, but also accounts
for the role of droplet sweeping via n(R). The second integral
captures the additional heat flux due to droplet coalescence and
sweeping.
[0101] In FIG. 13A, the heat flux ratio is plotted as a function
of a unique coalescence length scaled by the pinned base diameter
of the droplet for the cases where rp=1 [mu]m, 1.5 [mu]m and 2
[mu]m. Thus, the minimum allowable L corresponds to L/2rp=1 for
the three cases. FIG. 13 demonstrates that for rp=1 [mu]m, the CuO
surface degrades heat transfer performance in comparison to the
smooth surface over the entire range of allowable coalescence
lengths. For rp=1.5-2 [mu]m, qCuO/qF=1.13-1.25 at L/(2rp)=1, but
drops off steadily as L increases. This behavior is compared to a
hypothetical surface with the CuO structure height reduced to
[delta]CuO=100 nm. Here we see that the heat transfer behavior is
enhanced at L/(2rp)=1 for the three values of rp modeled, ranging
from 1.16<=qCuO/qF<=1.87. This result highlights the
important role of the parasitic thermal resistance associated with
the height of the structures. The inset of FIG. 13A shows the
predicted behavior for the three pinned regions sizes for the
average spacing identified in FIG. 11, (L)=4.42 [mu]m. The model
predicts qCuO/qF=0.37, 0.7 and 1.11 for rp=1 [mu]m, 1.5 [mu]m and
2 [mu]m, respectively.
[0102] The predicted behavior in FIG. 13A is a direct result of
the dominant thermal resistances as a function of droplet size for
the CuO nanostructured surface ([delta]CuO=1.5 [mu]m) compared to
a smooth hydrophobic surface for rp=1 [mu]m, 1.5 [mu]m and 2 [mu]m
(solid curves). The CuO surface shows an enhancement for
L/(2rp)->1 and rp<=1.5 [mu]m. This behavior is compared to
similar, hypothetical surface with the CuO height reduced to
[delta]CuO=100 nm (dashed curves). The hypothetical surface
demonstrates a wider range of enhancement (modeled conditions:
[Delta]T=0.034 K. pv=800 Pa). FIG. 13A inset shows the predicted
heat transfer behavior rp=1 [mu]m, 1.5 [mu]m and 2 [mu]m with
(L)=4.42 [mu]m. During early stages of growth (R<=6 [mu]m), the
conduction resistance ([psi]d) through the droplet is relatively
small compared to the conduction resistance through the pinned
base region and the curvature resistance. This explains the
significant effect of reducing the nanostructure height while
assuming identical contact angle behavior. Therefore, droplet
shedding at these radii isolates a regime of high growth rates (in
comparison to the later diffusion limited growth), but can only be
accessed in the jumping-droplet regime by reducing the
characteristic length-scale of the surface structures. In the
diffusion limited growth regime (R>=6 [mu]m), the performance
of the nanostructured CuO surface is penalized by the large
apparent contact angle of the droplets, which causes significant
thermal resistance due to the limited droplet basal contact area
in comparison to a droplet on the smooth condensing surface.
[0103] In FIGS. 13B-13C, the heat flux ratio is plotted as a
function of L/(2rp) for rp=1.5 [mu]m and [delta]CuO=1.5 [mu]m
(FIG. 13B) and [delta]CuO=100 nm (FIG. 13C) with 0.01
K<=[Delta]T<=5 0.05 K in steps of 0.01 K with constant
pv=800 Pa. FIG. 13D summarizes the results shown in FIGS. 13B-13C.
The values of qCuO/qp at L/(2rp)=1 (solid curves) and ¦qCuO/qF¦max
(dashed curves) for [delta]CuO=1.5 [mu]m (blue squares) and
[delta]CuO=100 nm (red circles) obtained from FIG. 13B and FIG.
13C, respectively. We can see that the jumping surface is more
strongly affected by the degree of subcooling in comparison to the
smooth surface. The strong effect of subcooling can be explained
by the fact that jumping droplets grow in size ranges from Rc up
to (L)/2( 1-10 [mu]m) where the curvature resistance is
appreciable during the majority of the droplet growth. However,
shedding droplets obtain most of their growth and heat transfer at
size ranges from Rc up to 1 mm) where the curvature resistance is
a smaller contribution to the thermal resistance. The result is a
heavier penalty paid by jumping droplets, especially at low
supersaturations. We observe this behavior in the model by
recalling that the heat transfer behavior of a jumping surface is
dictated solely by the first integral in Eq. 16, whereas in
conventional dropwise condensation the heat transfer behavior is
more heavily weighted by the second integral in Eq. 16 and the
important role of sweeping during droplet shedding. Thus, the
[Delta]T-(2Tsat[gamma]/Rhlv[rho]l) term in Eq. 13 plays a more
central role in the heat transfer behavior of jumping droplet
condensation surfaces.
CONCLUSIONS
[0104] A scalable synthesis method for creating unique oxide
nanostructures capable of providing sustained superhydrophobic
condensation was presented. Spatially random nucleation at low
supersaturations (S<=1.5) was observed using OM, suggesting the
role of randomly distributed defects in the thiol SAM coating on
the nucleation process. Observations of nucleation and growth
behavior using ESEM, coupled with a recently developed model of
the heat transfer process on superhydrophobic surfaces, suggests
that these surfaces may only become advantageous over a smooth
hydrophobic surface for coalescence-induced departure sizes below
~5 [mu]m (N>=1*10<10 >m<-2>) and for nucleation
densities corresponding to L/(2rp)->1 with rp>=1.5 [mu]m,
which is due predominantly to the increased resistance associated
with the large apparent contact angles demonstrated by drops on
the CuO surface and, to a lesser extent, the height of the
nanostructures and the assumption of comparable nucleation
densities for both the structured and smooth condensing surfaces.
This last assumption may be overly conservative given the large
roughness of the CuO surface. Indeed, we have recently
demonstrated, via macroscopic heat transfer measurements, that
these surfaces are capable of providing a 1.25* heat flux
enhancement compared to a conventional dropwise condensing
surface. See, Miljkovic, N., Enright, R., Nam, Y., Lopez, K., Dou,
N., Sack, J., and Wang, E. N., 2012, "Jumping-droplet-enhanced
condesation on scalable superhydrophobic nanostructured surfaces,"
Nano Lett., 10.1021/n1303835c1, which is included by reference in
its entirety. Good agreement between the data and the model was
obtained by taking the nucleation density on the CuO surface to be
three times larger than the corresponding smooth surface.
Furthermore, we note that, presently, the overall heat transfer
model does not account for the range of droplet separation
distances characteristic of a random distribution. This point
remains to be addressed in future studies.
[0105] By bounding the maximum nucleation density by the critical
L/l ratio, a maximum enhancement of ~1.6* has been predicted. In
addition to demonstrating the benefits of increased nucleation
density and smaller structure length scales, these results suggest
that the coalescence-induced jumping mechanism for droplet
departure should be studied in more detail to understand the
trade-off between efficient shedding and L/(2rp) ratios as they
approach unity, marking the transition to Wenzel behavior for the
partial wetting state. This work highlights some of the challenges
associated with realizing superhydrophobic surfaces that can
enhance condensational heat transfer, but also emphasizes
opportunities to engineer condensation behavior at nanometer
length scales.
[0106] Nomenclature
A Power law constant [m/s]
Ap Droplet base pinned area [m<2>]
b Power law exponent [-]
E Surface energy [J]
[Delta]E Change in surface energy [J]
E* Wetting-state energy ratio [-]
H Spherical segment height [m]
hi Interfacial heat transfer coefficient [W/m<2>.K]
hlv Latent heat [J/kg]
k Thermal conductivity [W/m.K]
l Characteristic structure spacing/pitch [m]
L Mean coalescence (nearest neighbor) length [m]
L Coalescence (nearest neighbor) length [m]
M Magnification factor [-]
N Nucleation density [m<-2>]
n Droplet number density [m ], refractive index [-]
N(R) Coalescence-dominated droplet size distribution [m<-2>]
n(R) Non-interacting droplet size distribution [m<-2>]
P Cumulative probability [-]
Pv Vapor saturation pressure [Pa]
Pw Saturation pressure corresponding to [Pa]
Q Flow rate [L/min]
q Heat transfer rate [W]
q' Heat flux [W/m<2>]
r Surface roughness[-]
rp Droplet pinned base radius [m]
R Droplet radius [m]
Specific gas constant [J/kg.K]
S Supersaturation (pv/pw[-]
t Time [s]
Tw Wall temperature [K]
TS Curvature-depressed vapor temperature [K]
[0139] [Delta]T Temperature difference between the liquid-vapor
interface and the droplet base [K]
W1 Single droplet work of adhesion [J]
W Two droplet work of adhesion [J]
[0142] Greek Symbols
[alpha] Condensation coefficient [-]
[gamma] Surface tension [N/m]
d Thickness/height [m]
[theta] Contact angle, x-ray diffraction angle [[deg.]]
[Delta][theta] Contact angle hysteresis [[deg.]]
[rho]1 Liquid density [kg/m<3>]
[tau] Sweeping period [s]
[nu][nu] Vapor specific volume [m<3>/kg]
[nu]l[nu] Change in specific volume between vapor and liquid
phases [m<3>/kg]
[phi] Solid fraction [-]
[psi] Thermal resistance [W/K]
[0154] Superscripts
CB Cassie-Baxter
W Wenzel
[0157] Subscripts
a Advancing
app Apparent
c Curvature, critical
d Droplet
e Equilibrium
eff Effective
F Flat
g Pinned liquid region under droplet
hc Hydrophobic coating
i Liquid-vapor interface
max Maximum
n Nanostructure
r Receding
sat Saturation
T Total
w Water
[0174] Acronyms
ESEM Environmental scanning electron microscope
NA Numerical aperture
RH Relative humidity
[0178] Other embodiments are within the scope of the following
claims.