Hojun Lee1, Soon-Bo Kang1, Hyunjae Yoo1, Hae-Ryung Lee1, Jeong-Yun Sun1,2. 1. Department of Materials Science and Engineering, Seoul National University, 1 Gwanak-ro, Gwanak-gu, 151-744 Seoul, Republic of Korea. 2. Research Institute of Advanced Materials (RIAM), Seoul National University, 1 Gwanak-ro, Gwanak-gu, 151-742 Seoul, Republic of Korea.
Abstract
The importance of chitosan has been strongly emphasized in literature because this natural polymer could not only remove heavy metal ions in water but also have the potential for recyclability. However, reversible phase transition and its dynamics, which are highlighting areas of a recycle process, have not been studied sufficiently. Here, we present dynamic studies of the dissolution as well as the gelation of a physically crosslinked chitosan hydrogel. Specifically, a one-dimensional gel growth system and an acetate buffer solution were prepared for the precise analysis of the dominant factors affecting a phase transition. The dissolution rate was found to be regulated by three major factors of the pH level, Cu2+, and NO2 -, while the gelation rate was strongly governed by the concentration of OH-. Apart from the gelation rate, the use of Cu2+ led to the rapid realization of gel characteristics. The results here provide strategies for process engineering, ultimately to determine the phase-transition rates. In addition, a microfluidic switch was successfully operated based on a better understanding of the reversible crosslinking of the chitosan hydrogel. Rapid gelation was required to close the channel, and a quick switchover was achieved by a dissolution enhancement strategy. As a result, factors that regulated the rates of gelation or dissolution were found to be useful to operate the fluidic switch.
The importance of chitosan has been strongly emphasized in literature because this natural polymer could not only remove heavy metal ions in water but also have the potential for recyclability. However, reversible phase transition and its dynamics, which are highlighting areas of a recycle process, have not been studied sufficiently. Here, we present dynamic studies of the dissolution as well as the gelation of a physically crosslinked chitosan hydrogel. Specifically, a one-dimensional gel growth system and an acetate buffer solution were prepared for the precise analysis of the dominant factors affecting a phase transition. The dissolution rate was found to be regulated by three major factors of the pH level, Cu2+, and NO2 -, while the gelation rate was strongly governed by the concentration of OH-. Apart from the gelation rate, the use of Cu2+ led to the rapid realization of gel characteristics. The results here provide strategies for process engineering, ultimately to determine the phase-transition rates. In addition, a microfluidic switch was successfully operated based on a better understanding of the reversible crosslinking of the chitosan hydrogel. Rapid gelation was required to close the channel, and a quick switchover was achieved by a dissolution enhancement strategy. As a result, factors that regulated the rates of gelation or dissolution were found to be useful to operate the fluidic switch.
Chitosan is a polysaccharide
obtained from
the deacetylation of chitin.[1−3] Based on its unique characteristics, such as hydrophilicity, biocompatibility,
and pH responsivity, a wide range of applications, such as drug delivery
and sensors, have been developed.[4−9] Especially, this polymer is also
capable of capturing heavy metal ions through a coordination bond,
so toxic metal ions in aqueous solutions can be easily removed by
a chitosan/metal-ion complex.[10,11] Furthermore, a recyclable
water purification system could be achieved using a reversible crosslinking
of the chitosan hydrogel. This indicates that chitosan is certainly
attractive because this natural polymer could reduce the environmental
concern as well.In relation to chitosan, recyclability could
be achieved by a reversible phase transition of physically crosslinked
polymers. For example, chitosan becomes dissolved when it is exposed
to an acid.[12−16] This is mainly
due to water solubility changes determined by the pH level. In detail,
chitosan polymers become soluble, accompanying the protonation of
NH2 below pH 6.3 and start to form a gel due to the deprotonation
of NH3+ above pH 6.3.[13−17] Similarly, coordination bonds between chitosan and
transition-metal ions are also related to the pH levels of the solutions.
For example, the chitosan/Cu2+ hydrogel was obtained above
pH 6.3, while the chitosan polymer was soluble in aqueous solutions
at the pH level below 6.3 (Figure ).[18] This is explained by
lone-pair electrons which are donated from NH2 to transition-metal
ions to facilitate their temporary sharing. Therefore, a fundamental
task is to determine the behavior of the polymer at different pH levels.
Figure 1
Illustration of the reversible
crosslinking of the physically crosslinked chitosan/Cu2+ hydrogel.
Illustration of the reversible
crosslinking of the physically crosslinked chitosan/Cu2+ hydrogel.With regard to the gelation of the chitosan hydrogel, previous
research studies were focused on the gelation rate using a one-dimensional
gel growth system in an alkali solution.[3,19−21] Nie et al. reported
that a high concentration of NaOH in an alkali led to an elevated
growth rate of the chitosan/Cu2+ hydrogel. Interestingly,
the rapid growth led to an oriented fibrous structure, while a discrete
multi-layer was obtained at a low growth rate.[19] Comparably, Dobashi et al. discussed the gelation speed
of chitosan polymers in alkalis with theoretical phase-transition
dynamics approaches.[20] However, more in-depth
studies are still required to clarify the factors as well as the mechanism
of chitosan gelation. Fortunately, the color shift of the chitosan/metal-ion
complexes is supposed to be a great hint to explain the gelation process.On the other hand, a few research groups reported chitosan derivatives
obtained by chemical modifications for the sake of enhancing the solubility
of the chitosan powder.[22−25] For example, Kim et al. suggested
that a catechol conjugation process could enhance the solubility of
modified chitosan powder in an aqueous solution at pH values up to
7.0.[22] However, previous works did not
discuss the case from a hydrogel to a solution as the concept of a
reversible phase transition. Besides, the effect of metal-ion binding
to the chitosan polymer on the dissolution has been barely studied
compared to the gelation. We believe that a comprehensive understanding
of the dissolution behavior will contribute to not only establishing
the recycle process but also expanding the application field of the
chitosan polymer.Here, we have conducted dynamic studies of
the dissolution as well as the gelation of physically crosslinked
chitosan/metal-ion complexes. Among metal ions, Cu2+ was
first considered due to the strong affinity of NH2 to Cu2+.[26,27] It is noteworthy that the hydrogels obtained
from the gelation test were directly applied to the dissolution test
in order to assume the recycling process. Furthermore, a one-dimensional
gel growth system and an acetate buffer solution were prepared for
the precise analysis of the dominant factors to determine the rates
of a phase transition. Lastly, a brief ligand chemistry was utilized
in order to understand the interaction between the polymer and metal
ions when a phase transition occurred. The effect of other metal ions
(Mn2+, Fe3+, and Ca2+) was also investigated
compared to Cu2+. At the end of the study, a microfluidic
switch was operated based on the reversible crosslinking of the chitosan/Cu2+ hydrogel.
Results and Discussion
Gelation of the Chitosan/Cu2+ Hydrogel
As
shown
in Figure a, the chitosan/Cu2+ hydrogel formation rate was analyzed through a one-dimensional
gelation system. A glass mold filled with the chitosan/Cu2+ solution and a clotting bath in which NaOH was dissolved were both
prepared. The chitosan/Cu2+ solution started to form a
gel as soon as the glass mold was immersed in the clotting bath. As
described in Figure d, a solution region under a gel layer decreased during gel growth
and the completely grown chitosan/Cu2+ hydrogel was finally
obtained. Then, a one-dimensional grown part was verified using the
rheological characterization. The values of the storage modulus were
always higher than those of the loss modulus regardless of Cu2+, which indicated that the hydrogel was successfully fabricated
(Figure S1). Besides, the gelation process
was visual because Cu2+ dissolved in the chitosan polymer
solution took part in the gelation through coordination bonding between
NH2 and Cu2+ considering the color change from
light blue (chitosan/Cu2+ solution) to deep blue (chitosan/Cu2+ hydrogel). The origin of different colors is that NH2 caused more splitting of the d-orbital of Cu2+ than water (H2O), as the N atoms in NH2 were
more electropositive than the O atoms in H2O. As a result,
the chitosan/Cu2+ hydrogel absorbed higher energy corresponding
to yellow light, the complementary color of deep blue.[28,29]
Figure 2
Gelation test of the chitosan/Cu2+ hydrogel:
(a) schematic description of a one-dimensional chitosan/Cu2+ hydrogel grown in contact with the NaOH aqueous solution. (b) Time
courses of the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.2) with concentrations of 2–20 wt % NaOH over
a time of 24 h. (c) Growth rate of chitosan/Cu2+ hydrogels
(Cu2+/NH2 = 0.0–0.5) with concentrations
of 2–20 wt % NaOH. (d) Photos of growing chitosan/Cu2+ hydrogel samples (Cu2+/NH2 = 0.0–0.5)
in contact with a 10 wt % NaOH aqueous solution. NH2 caused
higher energy absorption compared to H2O such that the
color change from light blue (chitosan/Cu2+ solution) to
deep blue (chitosan/Cu2+ hydrogel) occurred.
Gelation test of the chitosan/Cu2+ hydrogel:
(a) schematic description of a one-dimensional chitosan/Cu2+ hydrogel grown in contact with the NaOH aqueous solution. (b) Time
courses of the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.2) with concentrations of 2–20 wt % NaOH over
a time of 24 h. (c) Growth rate of chitosan/Cu2+ hydrogels
(Cu2+/NH2 = 0.0–0.5) with concentrations
of 2–20 wt % NaOH. (d) Photos of growing chitosan/Cu2+ hydrogel samples (Cu2+/NH2 = 0.0–0.5)
in contact with a 10 wt % NaOH aqueous solution. NH2 caused
higher energy absorption compared to H2O such that the
color change from light blue (chitosan/Cu2+ solution) to
deep blue (chitosan/Cu2+ hydrogel) occurred.For the chitosan polymers, they are able to become a physically
crosslinked gel when NH3+ is deprotonated to
NH2 on aqueous surfaces under alkaline conditions. Therefore,
the rate of deprotonation from NH3+ to NH2 should be a major factor affecting the chitosan hydrogel
formation outcome. As shown in Figure b, the time courses of gel growth indicated that an
increase in the concentration of NaOH led to rapid growth of the gel.
This can be explained by the higher diffusion rate of OH– through the grown hydrogel layer in order to deprotonate NH3+ at the sol/gel interface. The 2 wt % NaOH aqueous
solution required more than 72 h until gelation was fully complete
owing to the low diffusion rate of OH–. Apparently,
the chitosan gel growth rate strongly depended on the concentration
of NaOH. From a similar point of view, we predicted that a small amount
of acetic acid in chitosan solution could also be supportive in order
to promote the gel growth. According to the previous work reported
by Dobashi et al., a large amount of acetic acid in the chitosan solution
interrupted the chitosan gel growth due to a delay in the deprotonation
of NH3+ at the sol/gel interface.[20]On the other hand, the influence of the
concentration of Cu2+ (Cu2+/NH2 =
0.0–0.5) on the gel formation rate with the same concentration
of NaOH was mostly negligible (Figure c,d). This result was quite reasonable in that coordination
bonding can form only when lone-pair electrons are shared between
NH2 and Cu2+. Figure S2 clearly indicates that a chitosan/Cu2+ hydrogel with
a large amount of Cu2+ (Cu2+/NH2 =
1.0) also grew at a speed identical to that of a pure chitosan hydrogel
in the 20 wt % NaOH aqueous solution. Moreover, we investigated the
gelation behavior with different metal ions (Cu2+, Mn2+, Fe3+, and Ca2+) incorporated with
the chitosan polymer (Figure S3). In brief,
the chitosan/metal-ion gel (metal ion/NH2 = 0.2) growth
rate was undoubtedly accelerated when the concentration of NaOH became
high. For example, the chitosan/Fe3+ hydrogel grew faster
in 10 wt % NaOH aqueous solution compared to 5 wt % NaOH aqueous solution.
However, each chitosan/metal-ion hydrogel grew at a different rate,
which followed the order of Fe3+ ≈ Cu2+ > Mn2+ ≈ Ca2+. This was probably
caused by the change of affinity of NH2 to metal ions.
According the previous report, ethylenediamine favored Fe3+ and Cu2+ rather than Mn2+ and Ca2+.[27] This probably resulted in byproducts
such as Mn(OH)2 and Ca(OH)2, which interrupted
the diffusion of OH–. As explained by Nie et al.,
Ca(OH)2 precipitation within the chitosan hydrogel was
clearly observed.[19] The result indicated
that the strong affinity of NH2 to Cu2+ encouraged
the growth of the chitosan/Cu2+ hydrogel.Next, the
viscosity changes of the chitosan/Cu2+ complexes (Cu2+/NH2 = 0.0, 0.2) with sequential drops of aqueous
NaOH solutions (0–10 wt %) were measured (Figure ). As shown in Figure a, a rotary viscometer was
utilized and the viscosity was recorded until the spindle became unrotated
(Figure d,e). Even
though the viscosity measurement was inadequate in spatially heterogeneous
complexes, it could express a torque in the hydrogel, hindering the
rotation of the spindle. In detail, a piece of hydrogel nucleated
at the surface of the solution started to merge with each other and
interrupt the rotation of the spindle so that the rapid gel formation
led to a sharp increase in torque which was expressed by the viscosity.
Therefore, the viscosity fluctuations of the chitosan/Cu2+ complex may indicate how rapidly the gel growth proceeded. However,
we used representative viscosity measured in the whole sample because
it was impossible to detect the values of the heterogeneous regions
during gelation. Figure b,c clearly shows that the slope corresponding to the 10 wt % NaOH
aqueous solution was much steeper than the others (2 and 5 wt %).
This result indicates that gel characteristics were more quickly obtained
when a higher concentration of NaOH aqueous solution was added. This
can also be explained by the higher diffusion rate of OH–, resulting in rapid gel formation. It was quite analogous to the
gelation test in Figure in that the concentration of the NaOH aqueous solution determined
the speed of the gelation. However, the time scale was shorter compared
to Figure , because
the viscosity of the complexes exceeded a maximum range of the measurement
promptly during the gelation processes. Apart from the gel formation
rate, it was also found that the chitosan/Cu2+ complex
(Figure c) tended
to show higher viscosity than the pure chitosan hydrogel (Figure b) when the same
amount of NaOH aqueous solution was dropped. This was mainly due to
the stronger crosslinking of chitosan polymers with the help of Cu2+, which greatly hinders the rotation of the spindle. The
much higher storage modulus of the chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.2) than the pure chitosan hydrogel
(Cu2+/NH2 = 0.0) could be other evidence of
the strong crosslinking through coordination bonding (Figure S1).
Figure 3
Viscosity measurements
of the chitosan/Cu2+ hydrogel: (a) schematic description
of a rotary viscometer system using the chitosan/Cu2+ hydrogel
with sequential drops (0.3 mL/min) of a NaOH aqueous solution. (b)
Time courses of the pure chitosan hydrogel (Cu2+/NH2 = 0.0) at concentrations of 0–10 wt % NaOH. (c) Time
courses of the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.2) at concentrations of 0–10 wt % NaOH. (d) Photos
of the initial and final states of the pure chitosan hydrogel (Cu2+/NH2 = 0.0). (e) Photos of the initial and final
states of the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.2).
Viscosity measurements
of the chitosan/Cu2+ hydrogel: (a) schematic description
of a rotary viscometer system using the chitosan/Cu2+ hydrogel
with sequential drops (0.3 mL/min) of a NaOH aqueous solution. (b)
Time courses of the pure chitosan hydrogel (Cu2+/NH2 = 0.0) at concentrations of 0–10 wt % NaOH. (c) Time
courses of the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.2) at concentrations of 0–10 wt % NaOH. (d) Photos
of the initial and final states of the pure chitosan hydrogel (Cu2+/NH2 = 0.0). (e) Photos of the initial and final
states of the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.2).In conclusion, the higher diffusion
rate of OH– was the dominant driving force of the
physical gelation of chitosan/Cu2+ regardless of the concentration
of Cu2+. However, the Cu2+ within the chitosan
polymers accelerated the gaining of gel characteristics.
Dissolution of the Chitosan/Cu2+ Hydrogel
Before the dissolution test, chitosan/Cu2+ hydrogels with
various compositions (Cu2+/NH2 = 0.0–0.5)
were prepared using the 10 wt % NaOH aqueous
solution with the one-dimensional gelation system. That is to say,
the hydrogels obtained from the gelation test were applied to the
dissolution test as the concept of the recyclable process. Then, factors
that disintegrate a physically crosslinked chitosan/Cu2+ hydrogel were analyzed using 1.0 M acetate buffer solution system
with pH levels from 3.8 to 5.6 accompanied by mechanical stirring
(Figure a). This pH
range should be suitable for a dissolution test of the chitosan hydrogel
considering its pKa value of 6.3. Even
though citrate buffer solution could also provide the useful pH levels
from 3.0 to 6.2, the chitosan polymer was not dissolved well, probably
due to the strong ionic strength of the solution (Table S1).[30] Besides, the viscosity
was measured using a rotary viscometer in order to analyze the dissolution
quantitatively. In detail, 1.0 g of the chitosan hydrogel was immersed
in 10 mL of the buffer solution whose initial viscosity was 3.5 ±
0.7 mPa s. After that, the viscosity of the solution in which the
chitosan polymer disintegrated gradually increased until the hydrogel
was completely dissolved. Then, the viscosity uniformly converged
at 9.4 ± 1.0 mPa s because the final concentration of the chitosan
polymer was equal. Therefore, the convergence of the viscosity without
any residual chitosan/Cu2+ hydrogel indicated the complete
dissolution. Here, t90 was considered
as the dissolution time. As shown in Figure a, t90 was defined
as the time to reach 90% of the converging value after Weibull fitting.
Even though the heterogeneous regions should exist during dissolution,
we reported the viscosity measured in the solution representatively.
Figure 4
Viscosity measurements of the chitosan/Cu2+ hydrogel dissolution and solution color comparison: (a)
schematic
description of the chitosan/Cu2+ hydrogel dissolution using
an acetate buffer solution system with pH levels ranging from 3.8
to 5.6 and viscosity measurements. Here, t90, the time to reach 90% of the converging value after Weibull fitting,
was considered as the dissolution time. (b) Time courses of pure chitosan
hydrogel (Cu2+/NH2 = 0.0) dissolution in acetate
buffer solutions (pH 4 and 5 and NO2–/Cu = 0, ∞). (c) Time courses of chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.2) dissolution in acetate buffer
solutions (pH 4 and 5 and NO2–/Cu = 0,
9). (d) Time courses of chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.5) dissolution in acetate buffer solutions
(pH 4, 5 and NO2–/Cu = 0, 9). (e) Photos
of solutions with different colors after chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.0, 0.5) dissolution in acetate
buffer solutions (pH 5.6, NO2–/Cu2+ = 0–90). NO2– caused
higher energy absorption compared to NH2 such that the
Cu/NO2– aqueous solution was not bluish
but greenish. The residual chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.5) was observed when NO2– was not utilized at pH 5.6 (NO2–/Cu2+ = 0).
Viscosity measurements of the chitosan/Cu2+ hydrogel dissolution and solution color comparison: (a)
schematic
description of the chitosan/Cu2+ hydrogel dissolution using
an acetate buffer solution system with pH levels ranging from 3.8
to 5.6 and viscosity measurements. Here, t90, the time to reach 90% of the converging value after Weibull fitting,
was considered as the dissolution time. (b) Time courses of pure chitosan
hydrogel (Cu2+/NH2 = 0.0) dissolution in acetate
buffer solutions (pH 4 and 5 and NO2–/Cu = 0, ∞). (c) Time courses of chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.2) dissolution in acetate buffer
solutions (pH 4 and 5 and NO2–/Cu = 0,
9). (d) Time courses of chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.5) dissolution in acetate buffer solutions
(pH 4, 5 and NO2–/Cu = 0, 9). (e) Photos
of solutions with different colors after chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.0, 0.5) dissolution in acetate
buffer solutions (pH 5.6, NO2–/Cu2+ = 0–90). NO2– caused
higher energy absorption compared to NH2 such that the
Cu/NO2– aqueous solution was not bluish
but greenish. The residual chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.5) was observed when NO2– was not utilized at pH 5.6 (NO2–/Cu2+ = 0).Figure shows the
result of the dissolution test described in Figure . Contrary to gelation, the rate of protonation
from NH2 to NH3+ should be a major
factor affecting the chitosan hydrogel dissolution outcome. As shown
in Figure a, a decrease
in the pH level powered the dissolution rate significantly. Fortunately,
there was no distinct change in the pH level during the dissolution
of the chitosan/Cu2+ hydrogel due to the acetate buffer
solution.
Figure 5
Dissolution test of the
chitosan/Cu2+ hydrogel: (a) influence of Cu2+ within chitosan polymers
on the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.0–0.5) dissolution process. In this experiment, NO2– was not included in the acetate buffer
solution. (b) Influence of NO2– which
was dissolved in an acetate buffer solution (NO2–/Cu2+ = 0–90) on the chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.2) dissolution process.
Dissolution test of the
chitosan/Cu2+ hydrogel: (a) influence of Cu2+ within chitosan polymers
on the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.0–0.5) dissolution process. In this experiment, NO2– was not included in the acetate buffer
solution. (b) Influence of NO2– which
was dissolved in an acetate buffer solution (NO2–/Cu2+ = 0–90) on the chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.2) dissolution process.Next, two additional key factors which regulate the
dissolution rate of the chitosan/Cu2+ hydrogel were discovered.
The chitosan/Cu2+ hydrogel dissolved slowly as the concentration
of Cu2+ increased. Moreover, Cu2+ led to a lower
maximum pH level, at which point the chitosan/Cu2+ hydrogel
was completely disintegrated. For example, the chitosan/Cu2+ hydrogel (Cu2+/NH2 = 0.2, 0.5) remained swollen
at pH levels ranging from 5.2 to 5.6, where the pure chitosan hydrogel
could be perfectly soluble (Figure a). This implies that strong binding within the polymers
induced by coordination complexes required an intense driving force
in order to disintegrate. Fortunately, the metal-ion affinity of molecules
could be utilized for the purpose of enhancing the dissolution rate
as a ligand exchange from weaker molecules to stronger molecules generally
occurs in an aqueous solution.[31−33] Given the primary requirements such as metal-ion affinity, water
solubility, and pKa, NO2– was regarded as an excellent molecule. Theoretically,
N atoms in NO2–, which have electronegative
O atoms, show stronger metal-ion affinity than N atoms in NH2 such that Cu2+ prefers NO2– to NH2.[29,31−34] Despite the
fact that there are a few ligand molecules with stronger metal-ion
affinity than NH2, they were not suitable for chitosan/Cu2+ hydrogel dissolution (Table S2). For example, 2,2′-bipyridine is insoluble in water and
cyanide ions are weakly acidic with a pKa of 9.2. Here, NaNO2 was used as the source of NO2–, and its high solubility in water was
readily confirmed, more than 50 g/100 mL. As expected, NO2– dissociated from NaNO2 enhanced the
dissolution of the chitosan/Cu2+ hydrogel, and it is shown
in Figure b. In detail,
the dissolution rate increased dramatically as higher concentrations
of NO2– (NO2–/Cu2+ = 0–90) were utilized at the same pH level.
In addition, the maximum pH level at which a fully disintegrated solution
was obtained tended to be elevated when NO2– was applied. For example, the chitosan/Cu2+ hydrogel
(Cu2+/NH2 = 0.2) could be completely dissolved
at pH levels ranging from 5.0 to 5.6 when NO2– was utilized (NO2–/Cu2+ =
9–90), while it remained swollen at a pH level above 5.0 without
NO2– (NO2–/Cu2+ = 0). The strong effect of NO2– was investigated when other metal ions (Mn2+, Fe3+, and Ca2+) were utilized instead of Cu2+ (Table S3). For example, it took at most
50 min to dissolve the chitosan/Fe3+ hydrogel (Fe3+/NH2 = 0.2) at pH 5 with NO2– (NO2–/Mn2+ = 90), while
the same hydrogel was completely disintegrated after 450 min at pH
5 without NO2–. However, it was especially
notable that metal ions apparently affected the dissolution rate of
the chitosan/metal-ion hydrogels, probably due to the different affinity
of NH2 to metal ions.[26,27] For example,
the chitosan/Ca2+ hydrogel tended to be dissolved faster
than others, and this was probably because of the weak affinity of
NH2 to Ca2+ caused by the absence of the d-orbital
(not the transition metal).[19]Interestingly,
NO2– did not work when the pure chitosan
hydrogel was dissolved (Cu2+/NH2 = 0.0). For
example, a converging time at pH 5 was not significantly affected
by NO2– (NO2–/Cu2+ = 0, ∞), as shown in Figure b. This was a major difference in that NO2– (NO2–/Cu2+ = 9) shortens the converging time of the viscosity when
chitosan/Cu2+ (Cu2+/NH2 = 0.2, 0.5)
was dissolved (Figure c,d). Figure S4 shows the significant
effect of NO2– on the chitosan/Cu2+ hydrogel dissolution visually. This can be explained by
the interaction between the ligand molecules and the metal ions. In
detail, Cu2+ could be favorably extracted from strong binding
to chitosan polymers with the aid of NO2–, which has stronger metal-ion affinity compared to NH2,[29,31−34] while the pure chitosan polymer
was not affected by the ligand molecules. In fact, different colors
of the chitosan/Cu2+ solution which considerably depended
on the ligand molecules could be other evidence of the suggested mechanism.
As shown in Figure e, chitosan/Cu2+ dissolved in the CH3COOH/NO2– aqueous solution was light green in color,[35−37] while chitosan/Cu2+ dissolved in the CH3COOH aqueous solution was light blue.
The reason for the different colors can be explained as in Section . In practice,
the color of the Cu2+/NO2– (CuCl2/NaNO2) aqueous solution was greenish,
whereas the Cu2+/NH2 (ethylenediamine) aqueous
solution was bluish. However, the dissolution of the chitosan/Cu2+ hydrogel was not expected at a pH level above 6.3, even
with NO2–, mainly because chitosan polymers
could not become hydrated unless protonation occurred.In conclusion,
two other factors can clearly be involved when the chitosan/Cu2+ hydrogel was intended to be dissolved at a pH below 5.6.
Cu2+, which contributed to stronger crosslinking, led to
a slower dissolution, while NO2–, which
tended to attract Cu2+, accelerated the dissolution process
dramatically. Particularly, NO2– could
help the chitosan/Cu2+ hydrogel dissolve faster compared
to the pure chitosan hydrogel.
Reversible
Crosslinking for a Fluidic Switch
A fluidic
switch for water flow regulation was operated by means of the reversible
crosslinking of the chitosan/Cu2+ hydrogel. Figure S5 shows the simple construction of the
fluidic switch system which was operated via the reversible crosslinking
of chitosan/Cu2+ complexes.A water flow at a rate
of 30 mL/min was blocked only when gelation occurred at the connector
intersection. Then, all the water (30 mL/min) started to flow along
the detour route in 5 s (Figure a, blue symbol). In order to form the gel, the 0.02
g/mL chitosan/Cu2+ solution (Cu2+/NH2 = 0.2) and a 10 wt % NaOH aqueous solution were injected simultaneously
at a rate of 20 mL/min from opposite directions perpendicular to the
water flow line. A blue gel then successfully formed despite the continual
supply of water (Figure a). However, the fluidic switch did not work when an insufficient
amount of OH– was injected due to the slow gel formation
rate. For example, the 2 wt % NaOH aqueous solution did not result
in rapid gel formation such that water continued to flow with a slight
hindering of the flow rate (Figure a, red symbol).
Figure 6
Fluidic
switch test with reversible crosslinking of the chitosan/Cu2+ hydrogel: the water flow rate was fixed at 30 mL/min. (a) Close
test (gelation) with concentrations of 0–10 wt % NaOH. The
chitosan/Cu2+ solution and a NaOH aqueous solution were
injected simultaneously to form a gel. (b) Open test (dissolution)
with a CH3COOH (0, 10 wt %)/NO2– (0, 1.5 M) aqueous solution after the channel in (a) was blocked.
Fluidic
switch test with reversible crosslinking of the chitosan/Cu2+ hydrogel: the water flow rate was fixed at 30 mL/min. (a) Close
test (gelation) with concentrations of 0–10 wt % NaOH. The
chitosan/Cu2+ solution and a NaOH aqueous solution were
injected simultaneously to form a gel. (b) Open test (dissolution)
with a CH3COOH (0, 10 wt %)/NO2– (0, 1.5 M) aqueous solution after the channel in (a) was blocked.After the water flow was blocked
by successful gel formation, an open test was implemented. The water
flow rate increased instantly to 30 mL/min as soon as the gel was
removed when the CH3COOH/NO2– aqueous solution was steadily injected instead of the chitosan/Cu2+ solution and the NaOH aqueous solution. In addition, partially
dissolved chitosan polymers were readily found at the outlet. Interestingly,
a high concentration of CH3COOH and NO2– tended to shorten the operating time until the channel
opened completely, while pure water at a rate of 30 mL/min from the
water supply was not capable of removing the chitosan/Cu2+ hydrogel, which blocked the water flow (Figure b). This indicates that the chitosan/Cu2+ hydrogel not only was strong enough to endure the solvent
pressure but was also reversible for a fluidic switch application.
However, a small area of the aqueous surface in acidic conditions
and the absence of mechanical stirring led to a slow switchover from
closed to open. For example, it took more than 70 s until the channel
was fully opened even when 1.5 M of NO2– was utilized (Figure b, blue symbol). Note that Y-shaped connectors were used when injecting
the CH3COOH/NO2– aqueous solution
in order to verify the effect of the dissolution rate clearly without
pressure on the blocking gel.As a result, the fluidic switch
was demonstrated based on the reversible phase transition of the chitosan/Cu2+ hydrogel. Furthermore, factors that regulated the rates
of gelation or dissolution were found to be useful when operating
the fluidic switch.
Microfluidic Switch
For a space-saving device to be used
in narrow and sophisticated channels, the solution-based fluidic switch
system is expected to be advantageous compared to a mechanical valve
or a tiny gear.[38−43] As a demonstration, a seven-hole microfluidic channel
was fabricated using patterned PDMS on a glass substrate (Figure a,7e). The channel
structure was designed using a facile photolithography technique,
and the attachment of PDMS/glass was achieved after a plasma treatment
(Figure S6).[44−47] The final dimensions
of the channel were set to 300 μm × 50 μm (width
× depth), and an initial water flow check was implemented before
the switch test (Figure b).
Figure 7
Microfluidic
switch test: (a) seven-hole microfluidic channel using patterned PDMS
on glass. The channel dimensions were fixed as 300 μm (width)
and 50 μm (depth). (b) Initial water flow check with a rate
of 150 μL/min before the switch test. (c) The channel was closed
by the gelation of chitosan/Cu2+ near the intersection.
All the water started to flow along the detour route in 5 s. (d) The
channel opened in 15 s due to the dissolution of the chitosan/Cu2+ hydrogel using the CH3COOH/NO2– aqueous solution. (e) Microscopy image of the intersection
before the switch test. (f) Microscopy image of the intersection after
closing. The hydrogel is indicated by the white box to describe it
more clearly.
Microfluidic
switch test: (a) seven-hole microfluidic channel using patterned PDMS
on glass. The channel dimensions were fixed as 300 μm (width)
and 50 μm (depth). (b) Initial water flow check with a rate
of 150 μL/min before the switch test. (c) The channel was closed
by the gelation of chitosan/Cu2+ near the intersection.
All the water started to flow along the detour route in 5 s. (d) The
channel opened in 15 s due to the dissolution of the chitosan/Cu2+ hydrogel using the CH3COOH/NO2– aqueous solution. (e) Microscopy image of the intersection
before the switch test. (f) Microscopy image of the intersection after
closing. The hydrogel is indicated by the white box to describe it
more clearly.When the 0.005 g/mL chitosan/Cu2+ solution and
the 10 wt % NaOH aqueous solution were injected from both sides, all
the water (150 μL/min) started to flow along the detour route
in 5 s (Figure c). Figure f shows the chitosan/Cu2+ hydrogel part which directly formed near the intersection
immediately after the injection of the two solutions. In particular,
the gel was not removed until the acidic aqueous solution was injected
instead of the NaOH aqueous solution. For example, the CH3COOH/NO2– aqueous solution with a final
concentration of 10 wt %/1.5 M led to a smooth water flow without
any congestion in 15 s (Figure d). One aspect that differed from the fluidic switch described
in Section was
the quick switchover from closed to open. We considered that this
arose due to the low concentration of the chitosan/Cu2+ solution. In fact, a chitosan solution with high viscosity could
not be injected through the microfluidic channel. Therefore, we held
its concentration in the range from 0.02 to 0.005 g/mL. From a simple
estimation, there was approximately 25% of NH2 to be protonated
compared to the case described in Section .As a result, this demonstration
indicates that the reversible crosslinking of the chitosan/Cu2+ hydrogel can be applied to a microfluidic switch to regulate
a water flow readily. Furthermore, reproducibility as well as quick
switchover can be achieved in a microfluidic channel.
Conclusions
In summary,
dominant factors which influence the rates of the reversible crosslinking
of chitosan/Cu2+ hydrogels were studied experimentally.
Rapid gel formation could be achieved when the concentration of OH– increased regardless of the concentration of Cu2+, mainly due to the higher diffusion rate of OH–, which deprotonated NH3+ to NH2. Apart from the gelation rate, Cu2+ helped to realize
gel characteristics quickly. Contrary to gelation, a decrease in the
pH level was required to power the dissolution rate with the accelerated
protonation of NH2 to NH3+. Furthermore,
NO2–, which has strong affinity to metal
ions, helped to disintegrate the chitosan/Cu2+ hydrogel
well. This enhanced the dissolution rate of the chitosan/Cu2+ hydrogel. Even though the affinity of NH2 to metal ions
(Mn2+, Fe3+, and Ca2+) apparently
affected the dissolution as well as the gelation, a phase transition
of the chitosan/metal-ion hydrogel was similarly controlled by the
factors such as NaOH, pH, and NO2–. Finally,
a fluidic switch was operated via the reversible crosslinking of chitosan/Cu2+ hydrogels. The gel which formed at a high concentration
of OH– blocked the water flow perfectly. This gel
could not be removed until an acidic aqueous solution was injected.
Furthermore, NO2– dissolved in an acid
aqueous solution shortened the operating time from closed to open.
Moreover, a switch system could be successfully applied to a microfluidic
channel as well. We expect that a controllable microfluidic device
could be potentially applied to various fields such as hemostatic
systems and trace metal analysis. Besides, this study provides a better
understanding of the reversible crosslinking of the chitosan/metal-ion
hydrogel and helps with the preparation of comprehensive strategies
for the recycle process.
Experimental Section
Materials
Chitosan (Sigma, 448877) was used as a raw
hydrogel
material. The average viscosity of chitosan is 500 cp (1 wt % in 1
vol % CH3COOH aqueous solution), and the degree of deacetylation
is 75–85%. Acetic acid (CH3COOH), sodium acetate
(CH3COONa), sodium hydroxide (NaOH), copper chloride (CuCl2), manganese chloride (MnCl2), iron chloride (FeCl3), calcium chloride (CaCl2), and sodium nitrite
(NaNO2) were purchased from Daejung Chemical and Metals
Co., Ltd. and were of analytical reagent grade.
Gelation Test
Chitosan
solution was prepared by dissolving chitosan powder in 2 vol % of
a CH3COOH aqueous solution, with the final concentration
of chitosan fixed at 2 wt %. Then, various amounts of CuCl2 powder were added in order to form a chitosan/Cu2+ solution
with different molar ratios between Cu2+ and NH2 (Cu2+/NH2 = 0.0–0.5). Each solution
was added to a glass mold before being immersed in a clotting bath.
Clotting baths were prepared by dissolving various amounts of NaOH
pellets in deionized water, with the final concentrations held in
the range of 2–20 wt %. The growth of the chitosan/Cu2+ hydrogel was started when the chitosan/Cu2+ solution
was immersed into the NaOH clotting bath. Each of the glass molds
(2.5 mL of chitosan/Cu2+ solution) should be immersed in
at least 500 mL of the NaOH aqueous solution in order to ensure uniform
gelation. The chitosan/Cu2+ hydrogel growth rate was calculated
according to the gel thickness, which was measured every hour. The
color change from light blue (chitosan/Cu2+ solution) to
deep blue (chitosan/Cu2+ hydrogel) was observed when the
gelation proceeded.
Viscosity Measurements
The NaOH aqueous solution (2–10
wt %) as well as the chitosan/Cu2+ solution (Cu2+/NH2 = 0.0, 0.2) were prepared using the method described
in Section . 40
mL of the chitosan/Cu2+ solution was added to a glass mold,
and a spindle which was connected to a rotary viscometer (LVDV-II+,
Brookfield) was dipped into the solution. The viscosity of the complex
was recorded by adding an aqueous solution of NaOH with a speed of
0.3 mL/min.
Dissolution
Test
Chitosan/Cu2+ hydrogels were prepared using
the method described in Section except that the final concentration of NaOH was fixed
at 10 wt %. After gelation, chitosan/Cu2+ hydrogels were
rinsed with deionized water repeatedly and stabilized in a deionized
water bath for 24 h before the dissolution test. 1.0 M acetate buffer
solutions with pH levels ranging from 3.8 to 5.6 were prepared in
order to clarify the effect of the pH on the dissolution speed of
the chitosan/Cu2+ hydrogel. The relative concentrations
of CH3COOH and CH3COONa at each pH level were
calculated with the Henderson–Hasselbalch equation (pH = pKa + log{[A–]/[HA]}, pKa for acetic acid = 4.75).
The prepared buffer solutions were checked with a pH meter (Star A2116,
Thermo Scientific). Then, various amounts of NaNO2 powder
were added with different molar ratios between NO2– and Cu2+ (NO2–/Cu2+ = 0–90). The prepared chitosan/Cu2+ hydrogels were immersed in buffer solutions with a stirring speed
of 300 rpm at room temperature. Every 1.0 g of the chitosan/Cu2+ hydrogel should be immersed in 10 mL of the buffer solution
under each condition. In order to confirm the complete disintegration
quantitatively, the viscosity of the environmental buffer solution
was measured using a rotary viscometer. The viscosity gradually increased
as the chitosan hydrogel disintegrated into the buffer solution. Finally,
the complete dissolution was determined when the viscosity became
constant without any residual chitosan/Cu2+ hydrogel. Here, t90, the time to reach 90% of the converging
value after Weibull fitting, was considered as the dissolution time.
Fluidic Switching Test
A cross-shaped fluidic
test tube was assembled with transparent
polypropylene tubes and a four-way connector. Both tubes and the connector
are capable of operating in aqueous solutions ranging from the acidic
to basic pH level. The inner radius of the four-way connector was
1 mm. Water flowed through a vertical line at a rate of 30 mL/min.
Other tubes perpendicular to the water flow line were connected to
syringes with chitosan/Cu2+ solution and NaOH solution.
To close the water line, 0.02 g/mL of the chitosan/Cu2+ solution (Cu2+/NH2 = 0.2) and NaOH (0, 2,
10 wt %) aqueous solutions were simultaneously injected. The injection
rate for both syringes was fixed at 20 mL/min. The water flow rate
was calculated according to the amount of water which flowed in an
operating interval. To reopen the water line, a CH3COOH
(0, 10 vol %)/NO2– (0.0, 1.5 M) aqueous
solution was used. A Y-shaped bypass was connected to make a static
flow of CH3COOH/NO2– solution
near the blocking gel. 20 mL/min was used as an injection speed of
CH3COOH/NO2– solution.
Microfluidic Switching Test
A seven-hole microfluidic
channel was fabricated by patterning
PDMS (Sylgard 184, Dow Corning) on glass. The patterned PDMS was developed
by a facile photolithography technique in order to control the channel
structure. The final dimensions of the microfluidic channel were fixed
at 300 μm × 50 μm (width × depth). Permanent
bonding between PDMS and the glass was obtained via a plasma bonding
step after rinsing these surfaces with an acetone/ethanol solution.
Additional heat (60 °C) and pressure (6500 N/m2) were
applied to the PDMS/glass device for 48 h. The microfluidic switching
test was operated under similar conditions in Section , except for the final concentration of
chitosan/Cu2+ solution (0.005 g/mL, Cu2+/NH2 = 0.2) and flow rate (150 μL/min).