Xiufeng Li1, Philipp Erni2, Jasper van der Gucht1, Renko de Vries1. 1. Physical Chemistry and Soft Matter, Wageningen University and Research, Stippeneng 4, 6708 WE Wageningen, The Netherlands. 2. Firmenich Co, Rue Bergere 7, CH-1217 Geneva 2, Switzerland.
Abstract
Traditionally, complex coacervates of oppositely charged biopolymers have been used to form coatings around oil droplets for encapsulation of oil-soluble payloads. However, many proteins can form coacervates by themselves under certain conditions. Here, we revisit the well-known simple coacervates of prolamins such as zein in mixed solvents to explore whether they can be used for plant-based encapsulation systems. We show that, for zein in mixed water/propylene glycol (PG) solvents, we can encapsulate limonene droplets but only under specific conditions. We illustrate that this limitation is due to the very different physical properties of the simple zein coacervates as compared to those of the more extensively studied complex coacervates. Droplets of simple coacervates of zein can carry a significant net charge, whereas complex coacervates are usually close to being charge-balanced. In particular, we demonstrate that the spreading of zein coacervates at the interface of the droplets is thermodynamically favorable due to their extremely low interfacial tensions in both the dispersed (∼0.24 mN/m) and oil phases (∼0.68 mN/m), but the kinetics of coacervate droplet deposition and the interactions among coacervate droplets that oppose coacervate droplet coalescence are highly pH-dependent, leading to a sharp pH optimum (around pH 8) for capsule formation.
Traditionally, complex coacervates of oppositely charged biopolymers have been used to form coatings around oil droplets for encapsulation of oil-soluble payloads. However, many proteins can form coacervates by themselves under certain conditions. Here, we revisit the well-known simple coacervates of prolamins such as zein in mixed solvents to explore whether they can be used for plant-based encapsulation systems. We show that, for zein in mixed water/propylene glycol (PG) solvents, we can encapsulate limonene droplets but only under specific conditions. We illustrate that this limitation is due to the very different physical properties of the simple zein coacervates as compared to those of the more extensively studied complex coacervates. Droplets of simple coacervates of zein can carry a significant net charge, whereas complex coacervates are usually close to being charge-balanced. In particular, we demonstrate that the spreading of zein coacervates at the interface of the droplets is thermodynamically favorable due to their extremely low interfacial tensions in both the dispersed (∼0.24 mN/m) and oil phases (∼0.68 mN/m), but the kinetics of coacervate droplet deposition and the interactions among coacervate droplets that oppose coacervate droplet coalescence are highly pH-dependent, leading to a sharp pH optimum (around pH 8) for capsule formation.
Delivery
and release of active ingredients by microcapsules is of great interest
among others for pharmaceutical,[1] personal
care,[2] and food applications.[3] Many strategies are available to formulate microcapsules.
For instance, charged actives can be encapsulated by forming micelles
with oppositely charged polymers,[4] and
lipophilic molecules can be stabilized by surfactants or formulated
as Pickering emulsions.[5] In some cases,
the actives have also been covalently attached to the carrier materials.[6]A classic technique for the microencapsulation
of relatively hydrophobic active ingredients is by coating oil droplets
with a thick layer of coacervate (the polymer dense phase of a liquid–liquid
phase separated polymer system), which is subsequently cured to form
a shell.[7,8] This is an attractive technology since coacervation
can bring large amounts of polymers to interfaces and can produce
fine capsules with a very high loading efficiency (40–90%).[9]For both food and nonfood applications,
there is a strong interest in microencapsulation techniques that would
rely on just abundantly available plant biopolymers and still have
competitive performance. For most nonfood applications, the required
performance objectives can currently only be achieved using synthetic
polymers. On the other hand, for food applications, the dominant approach
to (coacervate-based) microencapsulation still involves the use of
animal proteins. A case in point are the well-studied complex coacervates
of weakly charged polysaccharides such as gum arabic with animal proteins
such as gelatin or whey protein.[10]Many of the most abundant plant storage proteins, such as the prolamins
and globulins in leguminous plants, are poorly soluble in water.[11] Additionally, the production of industrial plant
protein concentrates and isolates often involve processing steps that
lead to irreversible denaturation of (part of) the proteins.[12] As a consequence of these factors, it is difficult
to use proteins from these sources to formulate complex coacervates
that can be used for microencapsulation. Previous studies show that
some purified plant proteins (soy, pea, and wheat proteins) or certain
fractions of them can be formulated into complex or simple coacervates
for encapsulation.[13] Identifying suitable
processing approaches to use the less soluble plant storage proteins
for microencapsulation purposes would not only be interesting from
the point of view of sustainability but also because their more hydrophobic
nature may translate into better barrier properties.One approach
that has been quite extensively studied to use the less soluble plant
storage proteins as physical barriers around oil droplets in oil-in-water
emulsions is to create colloidal plant protein particles and use these
to formulate Pickering emulsions.[14,15] This requires
careful tuning of the hydrophobic/hydrophilic balance of the particles,
which has been achieved to some extent by also incorporating more
hydrophilic biopolymers.[16] For example,
the main storage protein of corn, zein, like other prolamins, is soluble
in aqueous ethanol binary solvents due to its unique amino acid composition,[17] and this solubility behavior can be exploited
to create colloidal zein particles by precipitation into aqueous (anti)solvents.[19] Velikov and co-workers reported that zein colloids,
synthesized by such an anti-solvent precipitation method, can stabilize
soybeanoil–water interfaces.[5] Furthermore,
colloidal stability of the emulsions itself could be improved by coating
zein colloids with gum arabic.[20] However,
Pickering stabilized emulsions usually rely on a large interfacial
energy barrier between the oil and water phase plus a precisely tuned
amphiphilicity of the particles. This implies that, with this method,
it is still challenging to encapsulate less hydrophobic and somewhat
smaller molecules (Mw ≈ 100–250
g/mol). Moreover, interfacial layers formed by discrete solid particles
remain porous for molecular-size payloads even at the maximum interfacial
packing fraction, limiting their suitability as an interfacial permeation
barrier.In the past, it has been found that some plant proteins,
under certain conditions, exhibit liquid–liquid phase separation
into a protein dense (often called coacervate) and a protein dilute
phase (often called excess phase). Simple coacervation is typically
found in a narrow range of solution conditions in between one- and
two-phase regions where dilute phases coexist with precipitates. For
prolamins in mixed solvents, coacervates are found over a narrow range
of solvent compositions.[17] Similarly, coacervation
of leguminous globulins occurs for a narrow range of pH and salt concentrations.[12]Therefore, a way forward in using the
more hydrophobic plant storage proteins for encapsulation purposes
might be to exploit the simple coacervates that they form. While encapsulation
by complex coacervates has been studied extensively, encapsulation
using simple coacervates has hardly been studied. Encapsulation of
oil droplets by simple coacervates of soy glycinin has been discussed
previously where core shell capsules were shown to be formed by slowly
inducing coacervation.[21]Complex
and simple coacervate droplets however have intrinsically very different
physical properties that will translate into a very different behavior
in the encapsulation process, and so far, these differences have not
been elucidated. For example, at the optimal mass ratio and pH, at
which the yield of coacervate is maximal, complex coacervate droplets
are nearly neutral,[10] so once they are
formed, they have a tendency to aggregate and coalesce. On the other
hand, simple coacervate droplets can carry net charges such that they
can be kinetically stable and resist coalescence. Also, due to their
hydrophobic nature, simple plant protein coacervates may tend to have
higher protein contents and hence can have higher viscosities, which
may also influence the kinetics of the encapsulation process.To investigate this issue, we here study the thermodynamics and kinetics
of wetting for simple coacervates of zein and demonstrate the encapsulation
of a low molecular weight hydrophobic molecule, limonene. Simple coacervation
of zein is well known to occur in ethanol–water binary solvents,[17] but in many cases, ethanol will not be a suitable
cosolvent in the encapsulation processes because it is miscible with
many low weight hydrophobic molecules to be encapsulated, such as
limonene. We therefore investigate propylene glycol as a cosolvent
and identify the condition of zein coacervation in mixed propylene
glycol–water solvents. Coacervation on oil droplets is induced
by slowly adding water, coming from the one-phase region at high propylene
glycol.We show that, for a broad range of conditions, zein
coacervate droplets thermodynamically want to wet the interface with
the limonene, but that for most conditions, they are kinetically prevented
from doing so. We also show, however, that special conditions do exist
for which the formation of thick zein coacervate layers around the
limonene droplets is kinetically possible.
Materials
and Methods
Materials
Zein from corn (Z-3625), propylene glycol
(W294004), (R)-(+)-Limonene (97%, 183164), Nile Red (7385-67-3), and
Oil Red O (O0625) were bought from Sigma-Aldrich. Hydrochloric acid
(1 and 0.1 N) and sodium hydroxide solutions (1 and 0.1 N) were used
to adjust pH and were from Merck. Ethanol absolute (AR) was purchased
from Biosolve BV. Milli-Q water was used in all experiments.
Phase
Diagram
Eight stock solutions (with different φPG) were prepared as follows: for each stock solution, 2 g
of zein was dissolved in 160, 140, 130, 120, 110, 100, 60, and 20
mL of PG (since it is already known that zein is soluble in pure PG
or 80% v/v PG with water[22]). Next, 40,
60, 70, 80, 90, 100, 140, and 180 mL of water were gradually added
to the zein solutions, respectively. In this way, the final volume
of each stock solution was 200 mL with a constant zein concentration
of 1% w/v. The pH of the stock solutions was adjusted to pH 10.0,
8.0, 5.3, and 2.6 using small amounts of hydrochloric acid (1 and
0.1 N) and sodium hydroxide solutions (1 and 0.1 N). The phase diagram
is constructed based on both microscopic images and macroscopic visual
observation of the sample vials after spinning at 4500 rpm for 30
min. From optical microscopy, samples are considered to be in the
two-phase coacervate region if they show transparent and spherical
microscopic droplets. Samples that are completely clear in optical
microscopy are considered to be in the one-phase region. Samples that
show irregular microscopic particles and aggregates are classified
as being in the two-phase precipitated region. Macroscopic visual
observation of sample vials after centrifugation is required to be
consistent with the microscopic observation: samples in the one-phase
region have no sediment and a clear supernatant. Samples in the two-phase
coacervate region have a viscous liquid phase, and samples in the
two-phase precipitated region have a powdery, solid precipitate.
Coacervate Yield and Protein Fraction
Solutions with 2 g
of zein dissolved in 40 mL of 80% v/v PG solvent were prepared. The
pH of the zein solutions was adjusted to different values (pH 2.92,
3.47, 4.02, 4.53, 5.17, 6.07, 6.46, 7.13, 7.63, 8.00, 8.50, 9.11,
9.48, and 9.96) using hydrochloric acid (1 and 0.1 N) and sodium hydroxide
solutions (1 and 0.1 N). Next, 10 mL of water was added to each solution
(this dilution changes the pH by no more than ±0.1), and all
samples were centrifuged at 4500 rpm for 30 min at room temperature
to accelerate the sedimentation of the zein coacervate. The zein coacervate
was weighed after removing the supernatant, and the samples were freeze-dried
to remove water. To completely remove PG, freeze-dried samples were
redispersed in 10 mL of 80% v/v ethanol with water, 30 mL of water
was added to precipitate zein into colloidal particles, and NaCl was
added until a final concentration of 100 mM, which leads to aggregation
of the colloidal zein. Next, the supernatant was removed using centrifugation.
The process was repeated at least three times to thoroughly remove
PG. Finally, samples were freeze-dried. The coacervate yield is the
final weight (after freeze drying) divided by the initial amount of
zein (2 g), and the mass fraction of protein in the coacervate is
determined by dividing the final weight (after freeze drying) by the
measured coacervate weight.
Rheology
Rheological measurements
were performed with an Anton Paar rheometer 501 equipped with a Peltier
element for temperature control. The temperature was controlled at
20 °C. A 25 mm plate–plate geometry with a gap size 0.5
mm was used. The coacervate samples with different pH (pH 7, 8, 9,
and 10) were prepared as described previously. In 65% v/v PG, the
supernatant was decanted after centrifugation and coacervate samples
were transferred onto the plate. We measured viscosity of the coacervate
samples as a function of a shear rate from 10–6 to
100 s–1 (viscosity was not measurable at shear rates
around 5 s–1 due to wall slip). We performed a gentle
pre-shear step (from 10–6 to 1 s–1) and waited for 5 min before all measurements to make samples as
homogeneous as possible and let samples stick to the plates. The shear
stress was monitored to confirm that there is no shear history effect
on the viscosity measurements.
Zeta Potential
Zeta potential was measured for zein colloids as a function of pH
using a Zetasizer NanoZS apparatus (Malvern Instruments, UK) equipped
with a 4 mW He-Ne 88 ion laser (λ = 633 nm). The zein colloids
were prepared by an antisolvent precipitation method. The hydrodynamic
size of the zein colloids was determined using dynamic light scattering,
and a diameter was found to be around 100 nm. The zein colloids were
dispersed in Milli-Q water, and various pH values (from pH 3.00 to
9.88) were achieved and adjusted by hydrochloric acid (1 and 0.1 N)
and sodium hydroxide solutions (1 and 0.1 N). Each sample was measured
three times at 20 °C, and the Smoluchowski equation was used
for converting measured mobilities to zeta potentials.
Pendant Drop
Measurements
Interfacial tensions between limonene and 65%
v/v PG at pH 7, 8, 9, and 10 were measured with a drop tensiometer
(Tracker from Teclis) using a reverse needle configuration. For all
measurements, the droplet area is constant at 15 mm2. Each
sample was measured 20 times with a data acquisition rate of one measurement
per second.
Surface Tension Determination via Capillary
Thinning
We obtained the interfacial tensions of coacervate
in its excess phase and in the oil phase using capillary thinning
experiments, which have been previously described by Dardelle and
Erni.[8] Capillary thinning experiments were
performed with the zein coacervate prepared at pH 7 as described above.
After centrifugation at 4500 rpm for 30 min, we reinjected the coacervate
in its supernatant or limonene on a glass surface, and the thinning
dynamics of filaments were recorded by a microscope camera and analyzed
with ImageJ. For coacervate filaments at 65% v/v PG (pH 7) or limonene,
we analyzed five samples by measuring the neck width as a function
of time.
Microcapsule Preparation
Typically, 2 g of zein was
dissolved in 80 mL of 80% v/v PG (65 mL of PG + 15 mL of water) in
a 250 mL beaker, and 1 mL of limonene with Oil Red O pre-dissolved
(for staining) was added to be encapsulated. A magnetic stirrer was
used to prevent limonene droplets from coalescing. The stir rate was
typically at 430 rpm unless specifically mentioned. Hydrochloric acid
(1 and 0.1 N) and sodium hydroxide solutions (1 and 0.1 N) were used
to adjust the solutions to the desired pH (pH 3, 4, 5, 7, 8, 9, and
10). Then, 20 mL of water was dropwise added by a syringe pump (1
mL/min). pH changes due to the addition of water were less than ±0.1
pH units.
CLSM (Confocal Laser Scanning Microscopy)
We used CLSM
to map the distribution of limonene droplets within capsules. Fluorescent
images were obtained using an inverted microscope system Eclipse Ti2
from Nikon. Limonene was stained with Nile Red (λex ≈ 550 nm, λem ≈ 630 nm). Capsules
for CLSM were synthesized at pH 8, as described above.
Results
and Discussion
Bulk Coacervate Properties
Ethanol–water,
as the mostly used binary solvent, has the optimal condition for zein
coacervate around 50% v/v ethanol (Figure S5). Zein has different solubility in PG–water. To use simple
zein coacervate in a PG–water binary solvent, we made a phase
diagram to locate precipitation, coacervation, and solution regions.
As Figure A shows,
the PG–water ratio has a strong impact on the solubility of
zein. For a φPG between 0 and 50% v/v, zein precipitates,
and between 50 and 70% v/v, we find a zein coacervate. Above 70% v/v,
zein becomes soluble. Representative optical microscopy images of
zein samples at pH 8 in the different regions are shown in Figure B–D. In part,
because the zein is not completely pure, phase boundaries are not
infinitely sharp, and we find narrow transition regions between the
different regions (see Figures S1 and S2). For example, we find both precipitate and coacervate at 55% v/v
for pH 2.6, 5.3, 8.0, and 10.0. In the coacervate region, the coacervate
yield decreases when the solvent is approaching 70% v/v PG. We choose
65% v/v PGzein coacervates for producing capsules because, for this
solvent composition, the supernatant is transparent and it has a good
yield of coacervate (by visual observation). In the pH range that
we have tested (from pH 2.6 to 10.0), we find that pH has only a minor
effect on the solubility and phase behavior of zein. At pH 2.6, the
zein coacervate disappears when φPG is around 60%
v/v. This may be attributed to the increasing solubility as a result
of the amide groups of glutamine and asparagine being hydrolyzed to
carboxyl groups.[17,23]
Figure 1
(A) Phase diagram for solubility of zein
in propylene glycol–water binary solvents. Precipitation (circle),
coacervation (triangle), and solution (square) are expressed as different
symbols with the coacervate region highlighted in red. Solid lines
denote the phase boundaries (note that the transitions are not very
sharp). (B–D) Representative optical microscopy images of zein
samples at pH 8 with different φPG of (B) 10%, two-phase,
precipitated region; (C) 65%, two-phase, coacervated region; and (D)
80%, one-phase region. Scale bars are 50 μm.
(A) Phase diagram for solubility of zein
in propylene glycol–water binary solvents. Precipitation (circle),
coacervation (triangle), and solution (square) are expressed as different
symbols with the coacervate region highlighted in red. Solid lines
denote the phase boundaries (note that the transitions are not very
sharp). (B–D) Representative optical microscopy images of zein
samples at pH 8 with different φPG of (B) 10%, two-phase,
precipitated region; (C) 65%, two-phase, coacervated region; and (D)
80%, one-phase region. Scale bars are 50 μm.Coacervate yield and protein fraction were determined at
various pH. As shown in Figure A, from pH 6 to 10, the decrease of coacervate yield is not
significant, but from pH 6 to 4, there is a clear decrease. Figure B shows the mass
fraction of protein in the coacervate. From pH 4 to 10, simple zein
coacervate has a high protein mass fraction between 30 and 40%. At
pH lower than 4, the protein mass fraction drops.
Figure 2
(A) Zein coacervate yield
at 65% v/v PG and (B) protein mass fraction in coacervate versus pH.
(A) Zein coacervate yield
at 65% v/v PG and (B) protein mass fraction in coacervate versus pH.We measured the viscosity of zein coacervates with
different pH at a wide range of shear rates. From Figure , we can see that zein coacervates
have a Newtonian behavior at low shear rates below 10–1 s–1. At higher shear rates, we observe shear thinning
followed by a high shear plateau viscosity. The magnitude of the viscosity
and the onset of shear thinning are both markedly influenced by pH:
at higher pH, when the zein molecules carry a higher net charge, viscosities
are lower and shear thinning sets in at lower shear rates. Possibly,
the increased net charge on the zein molecules decreases the cohesive
energy of the coacervates, leading to the observed changes in the
rheology. The absolute values of the viscosity that we found for the
zein coacervates in the PG/water binary solvents are orders of magnitude
larger than those found, for example, for gelatin-gum arabic complex
coacervates[8] and simple soy protein coacervates.[24] At least, in part, this is caused by the much
larger viscosity of the PG/water binary solvents. An empirical Cross
model was used to fit the flow curves, in order to determine the zero-shear
viscosities to be used to estimate interfacial tensions.
Figure 3
Viscosity of
zein coacervates (produced from 65% v/v PG) versus shear rate. The
red lines show Cross model fits. η = η∞ + (η0 – η∞)/[1 +
(Cγ̇)] where
η is the viscosity, C is the Cross model time
constant, γ̇ is the shear rate, and m is the Cross rate constant.
Viscosity of
zein coacervates (produced from 65% v/v PG) versus shear rate. The
red lines show Cross model fits. η = η∞ + (η0 – η∞)/[1 +
(Cγ̇)] where
η is the viscosity, C is the Cross model time
constant, γ̇ is the shear rate, and m is the Cross rate constant.
Surface Properties
We expect that the surface charge will
play a significant role in determining how the coacervate droplets
will coalesce. We cannot directly determine the electrophoretic mobility
of coacervate droplets in 65% v/v PG since the coacervate droplets
would have an extremely low mobility due to the high solvent viscosity,
and they would most likely also coalesce and sediment during the measurements.
Therefore, to obtain estimates of zein zeta potentials, we instead
used zein colloids and measured their zeta potential in water at pH
values from pH 3 to 9.88. Needless to say, this zeta potential may
deviate from that of zein coacervate droplets in PG/water solvents,
but we expect that at least the charge sign as a function of pH and
the order of magnitude of the zeta potential should be the same. Results
are shown in Figure . We find that the isoelectric point of zein is around pH 6.2, in
agreement with earlier results of Velikov et al. Below the isoelectric
point, zein is positively charged. From pH 6.2 to 10, the zeta potential
gradually changes from 0 to −60 mV. Below the isoelectric point,
from pH 6.2 to 4, there is a relatively sharper increase in the zeta
potential from 0 to +60 mV. The absolute values of the zeta potential
at pH 4 (+60 mV) and 10 (−60 mV) are very close. However, the
coacervate yield at pH 4 is much lower than that at pH 10. This suggests
that the zein behavior is not symmetric with respect to the distance
to the pI and that zein is more soluble in acidic conditions in the
PG/water binary solvent.
Figure 4
Zeta potential of zein colloids in water at
various pH. Error bars are indicating variations of three measurements
for each sample. A straight line is used to interpolate the data for
pH values around the isoelectric point from which we estimate an isoelectric
point of pI = 6.2.
Zeta potential of zein colloids in water at
various pH. Error bars are indicating variations of three measurements
for each sample. A straight line is used to interpolate the data for
pH values around the isoelectric point from which we estimate an isoelectric
point of pI = 6.2.From a thermodynamic
perspective, whether or not coacervate droplets wet limonene droplets
in 65% v/v PG is determined by three interfacial tensions, as described
by the spreading parameter S(25)where
L stands for limonene, P for 65% v/v PG, and C for coacervate. When S > 0, coacervate droplets wet the interface completely,
and when S < 0, coacervate droplets do not wet
the interface. From the pendant drop measurements shown in Figure , we know that γLP is between 11.5 and 12 mN/m at pH 7, 8, 9, and 10. Due to
the high viscosity of the zein coacervate and its low interfacial
tension, it is experimentally more difficult to measure the interfacial
tensions of zein coacervate with 65% v/v PG and limonene. Based on
experience, the interfacial tension between coacervate and its coexisting
phase is also expected to be very low. Spruijt and co-workers obtained
the interfacial tension between a coacervate of two charged polyelectrolytes
and its coexisting aqueous phase on the order of 100 μN/m.[26] Priftis and co-workers measured the interfacial
tension of polypeptide coacervates lower than 1 mN/m.[27] Low interfacial tension values (4.2 ± 0.3 mN/m) between
the coacervate and the continuous phase have also been obtained by
Bago Rodriguez and co-workers through a series of calculations.[28]
Figure 5
Interfacial tension between a limonene droplet and an
aqueous PG solution (65% v/v) at different pH values. The inset figure
shows the pendant drop setup with a reverse needle geometry.
Interfacial tension between a limonene droplet and an
aqueous PG solution (65% v/v) at different pH values. The inset figure
shows the pendant drop setup with a reverse needle geometry.Here, we estimate the interfacial tension (γCP and γCL) from capillary thinning dynamics
using a method adapted from extensional rheology.[29] Generally, coacervate filaments spontaneously break up
in a second fluid if their configuration is out of the static Rayleigh–Plateau
stability limit.[30] This process is driven
by the interplay of interfacial tension against viscous and elastic
stress of the coacervate filament. To apply this method, two conditions
need to be met. First, the visco-capillary time scale that determines
the speed of the thinning processneeds to be experimentally accessible. In this equation, η0 is the zero-shear viscosity, d0 is the initial neck width of the filament, and γ is the interfacial
tension. This method is particularly interesting for coacervates because
their low interfacial tension and their high viscosity[26,31] will lead to a large visco-capillary time scale. Second, the Ohnesorge
number Oh, which balances viscous against inertial
forces should be large, that is, inertia should be negligiblewhere Δρ
is the buoyant density of the filament in the surrounding fluid.Results for capillary thinning experiments are shown in Figure . Representative
microscopy images of the thinning process for a coacervate filament
in 65% v/v PG are shown in Figure A. Linear regression of the thinning dynamics (neck
width d versus time) suggests that the coacervate
filament behaves as a Newtonian fluid during thinning (Figure B). This is because if Oh ≫ 1, then a filament of Newtonian fluid should
undergo thinning at a constant velocity of ν ∼ γ/η0. Any elastic response of the filament would lead to thinning
with a nonconstant velocity; hence, elasticity can be neglected and
we can use the thinning model for a Newtonian fluidwhere d is the neck width
of a filament, γ is the interfacial tension, η0 is the zero-shear viscosity, and tc is
the critical time scale for filament breakup. For the numerical constant f, we use f = 0.1418 as found from Papageorgiou’s
similarity solution for a Newtonian fluid undergoing capillary thinning.[32] We use the zero-shear viscosity, η0 = 440 Pa·s at pH 7, as obtained from the rheology data
using the Cross model fit (Figure ). In contrast to capillary breakup extensional rheometry,
where the data are fitted such that the rheological properties can
be obtained for systems with a known interfacial tension, we use the
inverse approach here: based on the independently measured rheological
properties, we use the data here to calculate the interfacial tensions
of zein coacervate in its coexisting phase (∼0.24 mN/m) and
limonene (∼0.68 mN/m), see Figure C. Replicates of the filament thinning dynamics
in the excess phase or limonene oil are shown in Figures S3 and S4, respectively. Zein coacervates have a low
interfacial tension with their coexisting phases and a slightly higher,
but still very low, interfacial tension with the oil phase. Therefore,
at pH 7, the spreading parameter S is clearly larger
than zero such that complete wetting is thermodynamically favorable.
Figure 6
(A) Thinning
process of a coacervate filament in 65% v/v PG at different time scales;
the scale bar is 50 μm. (B) Thinning dynamics of a coacervate
filament. Neck width of the filament in panel (A) as a function of
time. The dashed line is a linear fit. (C) Calculated interfacial
tensions of coacervate filaments in polymer depleted 65% v/v PG phase
and limonene. Error bars are showing deviations among five measurements.
(A) Thinning
process of a coacervate filament in 65% v/v PG at different time scales;
the scale bar is 50 μm. (B) Thinning dynamics of a coacervate
filament. Neck width of the filament in panel (A) as a function of
time. The dashed line is a linear fit. (C) Calculated interfacial
tensions of coacervate filaments in polymer depleted 65% v/v PG phase
and limonene. Error bars are showing deviations among five measurements.
Capsule Formation
Next, we attempted
to create droplets of limonene surrounded by a thick coacervate layer
formed by the coalescence of coacervate droplets on the surface of
the limonene droplets. First, the oil is dispersed in a one-phase
zein solution at 80% PG. Coacervation is then induced by slowly adding
water, thus moving the system from the one phase region into the coacervate
region at 65% PG. The result of this process is shown in Figure for a range of pH
values. Starting at a low pH, at pH 3, no capsules are observed, just
the coexistence of oil droplets and very small coacervate droplets.
At pH 4, in addition to coacervate droplets in the bulk, we also observe
coacervate droplets that have adsorbed on the oil droplets but which
did not spread. Next, at pH 5 and 7, we observe macroscopic coacervate,
having engulfed almost all of the oil droplets. Moving further, at
pH 8, well-defined capsules of coacervate around oil droplets are
formed. Further increasing the pH leads to similar behavior as observed
at very low pH: at pH 9 and 10, coacervate droplets attach to the
surface of the oil droplets but do not spread.
Figure 7
Light microscope pictures
of capsules at (A) pH 3, (B) 4, (C) 5, (D) 7, (E) 8, (F) 9, and (H)
10. Limonene is stained with Oil Red O. The scale bars are 50 μm.
(G) Zoom-in image of a pH 9 sample, showing two examples of contact
angles between coacervate and oil droplets measured with ImageJ.
Light microscope pictures
of capsules at (A) pH 3, (B) 4, (C) 5, (D) 7, (E) 8, (F) 9, and (H)
10. Limonene is stained with Oil Red O. The scale bars are 50 μm.
(G) Zoom-in image of a pH 9 sample, showing two examples of contact
angles between coacervate and oil droplets measured with ImageJ.The nonequilibrium nature of the spreading behavior
of the coacervate is further illustrated by the zoom-in image of Figure G, for pH 9, where
we show two examples of coacervate droplets attaching to the oil droplets
with finite and very different contact angles (61 and 73°). Clearly,
even though thermodynamically favorable, the spreading of the zein
coacervate around the oil droplets does not occur easily due to kinetic
barriers.Our results clearly suggest that the electrostatic
repulsion between zein coacervate droplets play an important role
in determining the kinetics of coacervate droplet attachment to and
spreading on the oil droplets. For pH values far from the pI, the
charge on the coacervate droplets prevent both attachment to the surface
of the oil droplets and droplet fusion such that no capsules are formed.
For pH values very close to the pI, on the other hand, at a low droplet
charge, droplet fusion and spreading is easy and we end up with macroscopic
coacervates engulfing the oil droplets. Successful capsule formation
requires some droplet fusion while avoiding excessive coalescence,
such that there is an optimal charge on the coacervate droplets. In
principle, we would therefore expect pH windows for successful capsule
formation on both sides of the pI. Here, we have only found such a
pH window on the high side of the pI.
Influence of Local Shear
Fields in Capsule Formation
Having established that the capsule
formation is kinetically determined, we next investigate the role
of local shear fields during the capsule formation process. We hypothesize
that shear may aid in the coacervate droplet attachment if there are
kinetic barriers and may also promote spreading. To test this hypothesis,
we first produced capsules, as shown in Figure , using a fixed stirring speed of 430 rpm.
Next, capsules were stirred 10 more minutes at the same or higher
stirring rates (430, 760, and 1100 rpm). Results are shown in Figure .
Figure 8
Light microscope pictures
of capsules produced at pH 8 at a stirring rate of 430 rpm and further
stirred for 10 min at the same or higher stirring rates. (A) 430,
(B) 760, and (C) 1100 rpm. (D–F) Zoom-in figures of the above,
respectively. Scale bars are 200 μm.
Light microscope pictures
of capsules produced at pH 8 at a stirring rate of 430 rpm and further
stirred for 10 min at the same or higher stirring rates. (A) 430,
(B) 760, and (C) 1100 rpm. (D–F) Zoom-in figures of the above,
respectively. Scale bars are 200 μm.We find that capsules become smaller by the additional stirring at
higher rates (presumably due to break up), but also more spherical,
suggesting that, indeed, kinetic barriers for droplet spreading and
coalescence can be overcome by shear forces.The surface tension
of the zein coacervates with the 65% PG solvent is very low (order
10–4 N/m), whereas its viscosity is very high (order
100 Pa·s). This implies that a critical capillary number of Ca
≈ 1 corresponds to very low flow velocities of order 1 μm/s.
Hence, even low amounts of shear should, in principle, be able to
deform and break the zein coacervate droplets, although the kinetics
may be very slow due to the high viscosity. For limonene, on the other
hand, the viscosity is much lower than that of the coacervates, and
its interfacial tension with the 65% PG solvent is much higher; hence,
the coacervate droplets are much more likely to be deformed by shearing
than the limonene droplets.Finally, we used CLSM to more precisely
visualize the oil distribution within the capsules. Figure A shows a bright-field image
of a capsule, showing a large oil droplet covered by coacervate. Figure B shows the corresponding
CLSM image from which it is clear that there are in fact multiple
oil cores in the capsule. Figure C shows a 3D construction of a capsule, indicating
that this capsule contains a large oil core and some small oil droplets,
which were encapsulated during coacervate coalescence. This multinuclear
structure could lead to different release profiles with capsules only
containing a single core. If mononucleated capsules are desired, then
this could possibly be achieved by increasing the stirring rate.[33]
Figure 9
(A) Bright-field image of a capsule. (B) Corresponding
CLSM image of the capsule in panel (A). Scale bar is 10 μm.
(C) Three-dimensional construction of a capsule.
(A) Bright-field image of a capsule. (B) Corresponding
CLSM image of the capsule in panel (A). Scale bar is 10 μm.
(C) Three-dimensional construction of a capsule.
Conclusions
We have shown how simple coacervates of zein
can be used to create capsules around oil droplets. As opposed to
the generally much more hydrophilic animal proteins usually used to
formulate complex coacervates for encapsulation, these plant proteins
are quite water-insoluble and this may have advantages in terms of
barrier properties. Here, we have used zein biopolymers as an example
and found that, while thermodynamically, the spreading of zein coacervates
droplets on oil droplets is highly favorable, the process is kinetically
difficult. As a result of the high protein concentration and the high
viscosity of PG, the dynamics of coacervate droplet spreading is extremely
slow. In addition, simple zein coacervate droplets carry net charges,
leading to electrostatic barriers, preventing droplet attachment to
the surface of the oil droplets and the fusion of coacervate droplets.
Also, if the droplet charge is too low, then the rapid macroscopic
phase separation of the zein ensues and no capsules are formed either.Nevertheless, by precisely tuning the charge on the coacervate
droplets via the pH, it is possible to identify a window of solution
conditions for which capsule formation is kinetically possible. We
find that capsules can be formed at pH 8 and 65% v/v PG. Furthermore,
we showed that high local shear fields can provide hydrodynamic forces
to overcome some of the kinetic barriers and lead to smaller, more
spherical capsules. Note that many oils (for example, soybeanoil,
coconut oil, and medium-chain triglycerides) are more hydrophobic
than limonene. For all of these, the interfacial tension with PG–water
should be higher, making the wetting process even more favorable.
With limonene, we have therefore chosen a challenging case such that
we expect the procedure should work for a wide range of other oils,
too.While, here, we focused on the thermodynamics and kinetics
of the formation of zein coacervate layers around oil droplets, for
real applications, the mechanical properties of such capsules will
need to be further enhanced by cross-linking. Also, it will be very
interesting to see whether, indeed, barrier properties for cross-linked
zein capsules are notably different from capsules produced from, e.g.,
gelatin-gum arabic complex coacervates.[7] Finally, since many plant seed storage proteins form simple coacervates,
our results point to many new opportunities for using plant proteins
for encapsulation.