Mao Chen1, Yuwei Gu1, Awaneesh Singh2, Mingjiang Zhong3, Alex M Jordan4, Santidan Biswas2, LaShanda T J Korley4, Anna C Balazs2, Jeremiah A Johnson1. 1. Department of Chemistry and Department of Chemical Engineering, Massachusetts Institute of Technology , 77 Massachusetts Avenue, Cambridge, Massachusetts 02139, United States. 2. Chemical Engineering Department, University of Pittsburgh , Pittsburgh, Pennsylvania 15261, United States. 3. Department of Chemistry and Department of Chemical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Cambridge, Massachusetts 02139, United States; Department of Chemistry and Department of Chemical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Cambridge, Massachusetts 02139, United States. 4. Department of Macromolecular Science and Engineering, Case Western Reserve University , Cleveland, Ohio 44106, United States.
Abstract
Light-initiated additive manufacturing techniques typically rely on layer-by-layer addition or continuous extraction of polymers formed via nonliving, free radical polymerization methods that render the final materials "dead" toward further monomer insertion; the polymer chains within the materials cannot be reactivated to induce chain extension. An alternative "living additive manufacturing" strategy would involve the use of photocontrolled living radical polymerization to spatiotemporally insert monomers into dormant "parent" materials to generate more complex and diversely functionalized "daughter" materials. Here, we demonstrate a proof-of-concept study of living additive manufacturing using end-linked polymer gels embedded with trithiocarbonate iniferters that can be activated by photoinduced single-electron transfer from an organic photoredox catalyst in solution. This system enables the synthesis of a wide range of chemically and mechanically differentiated daughter gels from a single type of parent gel via light-controlled modification of the parent's average composition, strand length, and/or cross-linking density. Daughter gels that are softer than their parent, stiffer than their parent, larger but with the same modulus as their parent, thermally responsive, polarity responsive, healable, and weldable are all realized.
Light-initiated additive manufacturing techniques typically rely on layer-by-layer addition or continuous extraction of polymers formed via nonliving, free radical polymerization methods that render the final materials "dead" toward further monomer insertion; the polymer chains within the materials cannot be reactivated to induce chain extension. An alternative "living additive manufacturing" strategy would involve the use of photocontrolled living radical polymerization to spatiotemporally insert monomers into dormant "parent" materials to generate more complex and diversely functionalized "daughter" materials. Here, we demonstrate a proof-of-concept study of living additive manufacturing using end-linked polymer gels embedded with trithiocarbonate iniferters that can be activated by photoinduced single-electron transfer from an organic photoredox catalyst in solution. This system enables the synthesis of a wide range of chemically and mechanically differentiated daughter gels from a single type of parent gel via light-controlled modification of the parent's average composition, strand length, and/or cross-linking density. Daughter gels that are softer than their parent, stiffer than their parent, larger but with the same modulus as their parent, thermally responsive, polarity responsive, healable, and weldable are all realized.
With nearly
40 years of extensive
development, photoinitiated free radical polymerization is unequivocally
a robust and versatile technique for material fabrication with numerous
applications in coatings, adhesives, microelectronics, optics, and
biomaterials.[1] In particular, new three-dimensional
(3D) printing systems that leverage the speed and oxygen sensitivity
of free radical polymerization have enabled remarkable advances in
additive manufacturing.[2,3] Despite these demonstrated successes,
the chemistry of free radical polymerization has limitations that
preclude certain potentially desirable features of 3D printed objects.
Most notably, polymers produced via free radical processes cannot
be reinitiated to induce chain extension (Figure a); these polymers are not “living”.[4] Thus, in the context of additive manufacturing,
materials made via layer-by-layer or continuous solid–liquid
interface methods that use traditional free radical polymerization
cannot be subsequently reactivated after fabrication to introduce
new monomers and/or functionality in a living fashion.
Figure 1
Comparison of traditional
light-induced additive manufacturing
and proposed living additive manufacturing. (a) Free radical polymerization
produces materials with chains that cannot be reactivated for insertion
of new monomers. Though extremely well developed, these methods cannot
achieve homogeneous modification of already printed objects. (b) Herein,
we develop a living additive manufacturing approach wherein parent
objects comprised of dynamic covalent polymer networks are reactivated
via a photoinduced living radical polymerization to generate daughter
objects with homogeneous network modifications. These daughter objects
of varying composition can be welded together to form increasingly
complex progeny with spatially defined stimuli-responsive behaviors.
Comparison of traditional
light-induced additive manufacturing
and proposed living additive manufacturing. (a) Free radical polymerization
produces materials with chains that cannot be reactivated for insertion
of new monomers. Though extremely well developed, these methods cannot
achieve homogeneous modification of already printed objects. (b) Herein,
we develop a living additive manufacturing approach wherein parent
objects comprised of dynamic covalent polymer networks are reactivated
via a photoinduced living radical polymerization to generate daughter
objects with homogeneous network modifications. These daughter objects
of varying composition can be welded together to form increasingly
complex progeny with spatially defined stimuli-responsive behaviors.An alternative living
additive manufacturing approach
could involve the spatiotemporal insertion of monomers and/or cross-linkers
directly into the strands of an existing polymeric network to convert
the “parent” network into a new “daughter”
network with altered shape, composition, and properties (Figure b). To realize living
additive manufacturing, a highly controlled, light-regulated[5−9] living polymerization capable of repeated insertion of monomers
into dynamic covalent polymer networks without side reactions or significant
termination is needed. Though there are many examples where light
is used to alter the composition, structure, shape, motion, dynamics,
and mechanics of polymer networks,[10−21] often using sulfur-based functional groups as dynamic covalent bonds,[22−30] none have been proven capable of living insertion of new monomers
to achieve additive growth of the material as described in Figure b.To our knowledge,
there are only two reports wherein photoinduced
insertion of monomers into polymer network strands is investigated
experimentally;[31,32] neither involves living chain
growth (note: we have also investigated such processes using simulations
that neglect termination reactions and thereby model a living polymerization[33]). In 2013, we reported the photoinduced insertion
of N-isopropylacrylamide (NIPAAM) into the strands
of polymer networks using an ultraviolet-light initiated polymerization
based on trithiocarbonate iniferters (TTCs).[31] Though this polymerization displayed living behavior when conducted
in solution, the corresponding gel growth was not well controlled.
This limitation was the direct result of the mechanism of UV-induced
polymerization using TTCs, which involves photolysis of a TTC to generate
a propagating carbon-centered radical and an unstable trithiocarbonate
radical. In solution, these reactions display living behavior when
a low light intensity is used, and when the concentration of TTC is
high (∼mM regime); this scenario ensures that the unstable
TTC radical can be stabilized by another equivalent of nonphotolyzed
TTC.[34] In our experience, when TTCs were
embedded within polymer network strands, regions of the sample near
the surface absorbed the most light and underwent uncontrolled polymerization/decomposition;
it was impossible to achieve uniform, living chain growth throughout
the entire network. In 2015, Kloxin and co-workers reported a similar
study using UV-activation of dithiocarbamate iniferters embedded in
polymer network strands.[32] Here, dimethacrylate
cross-linkers were inserted into the network strands under UV irradiation.
No discussion of the livingness of this reaction was provided, but
given the close mechanistic relationship to our previous work[31] it is unlikely that the process was highly controllable
at the molecular level.Because the limitations of the above
systems are the direct result
of the UV-induced photolysis mechanism of polymerization,[6] and the resulting unstable trithiocarbonate radical
intermediates, we sought a living polymerization process capable of
monomer insertion into polymer chains that would proceed via different
reactive intermediates. Recently, inspired by developments in organic
synthesis,[35] a plethora of photoredox catalyzed
polymerization reactions have emerged.[6] These methods include variants of atom-transfer radical polymerization
(ATRP),[36−41] reversible addition–fragmentation chain transfer (RAFT)/iniferter
polymerization,[42−45] ring-opening metathesis polymerization (ROMP),[46] and cationic polymerization.[47,48] In 2015, inspired
by the work of Boyer and co-workers,[42] we
reported on the solution-phase photocontrolled radical polymerization
of several acrylate and acrylamide monomers mediated by symmetric
TTC iniferters and the photoredox catalyst 10-phenylphenothiazine
(PTH).[43] We found that this polymerization
greatly outperformed the traditional UV-induced direct TTC photolysis
iniferter polymerization allowing the synthesis of polymers with higher
molecular weights and greater control over molecular weight distributions.
This increased control is thought to arise from differences in the
reaction mechanisms: in the PTH-catalyzed process, photoinduced single
electron transfer from PTH to the TTC induces the formation of a propagating
radical, a TTC anion, and the PTH radical cation; the unstable
TTC radical that leads to irreversible termination in the UV-photolysis
method is not produced. Furthermore, because this photoredox
polymerization involves excitation of a catalytic amount of PTH using
visible light, it is possible to achieve uniform irradiation and living
polymerization over larger reaction volumes. We reasoned that these
features, made possible by the use of a distinct photoredox catalysis
mechanism, could be harnessed to realize our goal of living additive
manufacturing as described in Figure b.Herein, we report proof-of-concept studies
of living additive manufacturing
via photoredox catalyzed growth (PRCG) of uniform polymer gels (Figure a). PRCG begins with
the synthesis of a homogeneous end-linked gel bearing TTC iniferters
within the network strands. This “parent” gel is then
exposed to a solution containing PTH photocatalyst, monomers (M),
and cross-linkers (CL). Irradiation with blue LED light excites PTH
in solution and initiates the living insertion of M and CL from solution
into the network strands following the photoredox catalysis mechanism
described in Figure b. This process avoids the formation of unstable TTC radicals; it
enables the living insertion of new functionality into the strands
of polymer networks (e.g., Figure b) to produce diverse daughter materials. We use PRCG
to control network composition and mesh size, parameters that synergistically
dictate the macroscopic properties of gels.[49−53] Thus, we are able to produce daughter gels with homogeneously
altered compositions and either increased stiffness, decreased stiffness,
or no net change in stiffness compared to the parent gel, all outcomes
that could not be achieved using traditional free radical polymerization
(Figure a). Furthermore,
progeny gels with unique compositions, shapes, and patterned behaviors,
such as temperature and polarity responsiveness, are fabricated by
photowelding of daughter gels with different compositions. To validate
the living nature of PRCG, we conducted gel disassembly experiments
and simulations, showing that the macroscopic gel properties achieved
experimentally (such as shear storage modulus (G′)
and swelling ratio (Ww/Wd)) can be directly traced to PRCG-induced uniform increases
in the molecular weight between network junctions.
Figure 2
Photoredox catalyzed
growth (PRCG) of cross-linked polymer gels.
(a) General schematic for controlling polymer network structure by
PRCG. Monomers (M) and cross-linkers (CL) can be directly incorporated
into the network strands via a living photoredox catalyzed process.
(b) Proposed mechanism of PRCG polymerization using a suitable photocatalyst
(10-phenylphenothiazine, PTH) and a network comprised of strands bearing
trithiocarbonate (TTC) iniferters. Blue LED light excites PTH molecules
in solution and leads to photoinduced electron transfer from PTH*
to the network-bound TTCs. Strand cleavage produces a propagating
strand (green), a strand with a stable TTC anion (blue), and the PTH
radical cation in solution (purple). In the presence of monomers (M)
or cross-linkers (CL), the propagating strand can grow; it can also
undergo degenerative chain transfer (“RAFT process”)
with adjacent nonactivated network strands. Turning the light source
“OFF” leads to recombination of the cleaved strands
via back electron transfer to the PTH radical cation, thereby resulting
in net photocontrolled insertion of new M and CL into the network
in a living fashion.
Photoredox catalyzed
growth (PRCG) of cross-linked polymer gels.
(a) General schematic for controlling polymer network structure by
PRCG. Monomers (M) and cross-linkers (CL) can be directly incorporated
into the network strands via a living photoredox catalyzed process.
(b) Proposed mechanism of PRCG polymerization using a suitable photocatalyst
(10-phenylphenothiazine, PTH) and a network comprised of strands bearing
trithiocarbonate (TTC) iniferters. Blue LED light excites PTH molecules
in solution and leads to photoinduced electron transfer from PTH*
to the network-bound TTCs. Strand cleavage produces a propagating
strand (green), a strand with a stable TTC anion (blue), and the PTH
radical cation in solution (purple). In the presence of monomers (M)
or cross-linkers (CL), the propagating strand can grow; it can also
undergo degenerative chain transfer (“RAFT process”)
with adjacent nonactivated network strands. Turning the light source
“OFF” leads to recombination of the cleaved strands
via back electron transfer to the PTH radical cation, thereby resulting
in net photocontrolled insertion of new M and CL into the network
in a living fashion.
Results and Discussion
Living Insertion of NIPAAM into TTC-Containing
Parent Polymer
Networks via PRCG
We first investigated the feasibility of
using photoredox catalyzed activation of TTCs for living polymer growth
in solution and in parent gel networks bearing TTC groups. As expected,
exposure of a solution of NIPAAM and a TTC iniferter to blue LED light
(410 nm, 0.20 mW/cm2) in the presence of PTH catalyst led
to highly controlled polymer growth (see Section C in Supporting Information for details of solution
polymerization studies). The molecular weight of the polyNIPAAM product
increased linearly with monomer conversion as monitored by gel permeation
chromatography (GPC). When no PTH was added, the NIPAAM conversion
remained below 5% after 24 h of irradiation.Next, parent networks
(gel I, Figure a) containing TTC groups embedded in each strand were formed
via strain promoted alkyne–azide cycloaddition (SPAAC)[54−56] coupling of a four-arm polyethylene glycol (PEG) star polymer terminated
with dibenzocyclooctyne (Tetra-DBCO-PEG) and a bis-azide TTC (bis-N3-TTC) (Figure a) in the presence of PTH and NIPAAM (0.75 mM and 2.5 M, respectively;
see Methods section for details). Then, the
parent gels were exposed to blue LED irradiation (method A, Figure a) to induce insertion
of NIPAAM into the network strands following the mechanism outlined
in Figure b. NIPAAM
conversion was determined by proton nuclear magnetic resonance (1H NMR) analysis of extracted sol fractions (see section D
in Supporting Information for experimental
operation). By varying the exposure time, five daughter gels (II-a
to II-e, Figure ),
each with a different NIPAAM composition (up to 73% NIPAAM conversion),
were produced.
Figure 3
Living additive manufacturing via PRCG insertion of NIPAAM
into
a parent PEG-TTC network. (a) Parent network design. Gelation is achieved
by SPAAC click chemistry. PRCG is conducted in the presence of monomer
and PTH under blue LED irradiation. (b) Experimental storage modulus G′ (blue curve) and simulated results of inverse
of average chain length (1/Mc) between
junctions (red curve) as a function of monomer conversion in PRCG.
(c) Swelling ratio (blue curve). Defined as Ww/Wd, where Ww is the weight of a sample swollen in pure water at 20 °C; Wd is the weight of this sample in the dry state)
and simulated average chain length between network junctions, Mc, (red curve) as a function of monomer conversion.
(d) Optical images of parent gel I and daughter gels II-a to II-e swollen in pure water at 20 °C.
Living additive manufacturing via PRCG insertion of NIPAAM
into
a parent PEG-TTC network. (a) Parent network design. Gelation is achieved
by SPAAC click chemistry. PRCG is conducted in the presence of monomer
and PTH under blue LED irradiation. (b) Experimental storage modulus G′ (blue curve) and simulated results of inverse
of average chain length (1/Mc) between
junctions (red curve) as a function of monomer conversion in PRCG.
(c) Swelling ratio (blue curve). Defined as Ww/Wd, where Ww is the weight of a sample swollen in pure water at 20 °C; Wd is the weight of this sample in the dry state)
and simulated average chain length between network junctions, Mc, (red curve) as a function of monomer conversion.
(d) Optical images of parent gel I and daughter gels II-a to II-e swollen in pure water at 20 °C.To assess the impact of PRCG on
the daughter gel properties, G′ values for
water-swollen daughter hydrogels II-a to II-e and parent hydrogel I were measured using oscillatory
rheometry. As shown in Figure b, G′ gradually decreased from 4400
to 900 Pa as monomer conversion
increased, which is expected given that insertion of NIPAAM leads
to a decrease in cross-linking density (Figure a). Irradiation of the parent gel I in the absence of either NIPAAM or PTH or both afforded no change
in G′ (see Section D in Supporting Information). Simulation of the PRCG monomer insertion
process using dissipative particle dynamics indicated that the chain
length between network junctions (Mc)
increased as the conversion increased (red curve, Figure b); the inverse of Mc followed a similar trend as the measured G′ (see section F in Supporting Information for simulation).[33] The
similarity between these two curves can be explained using rubber
elasticity theory, which states that G′ is
proportional to the average chain length between junctions (neglecting
topological defects).[57,58] Since daughter materials II-a to II-e differ from each other in terms
of NIPAAM conversion, a more detailed treatment that takes into account
the polymer volume fraction in the preparation state (ϕ0) and in the swollen state (ϕ) is provided in Figure S16 (section G of Supporting Information).
This corrected G′ also shows very good agreement
with the simulated results. To examine the effect of the newly incorporated
monomers on the swelling behavior of gels in aqueous media, the swelling
ratios (Ww/Wd) were measured for parent gel I and daughter gels II-a to II-e. As illustrated in Figure c, when the monomer conversion
increased from 0 to 73%, the Ww/Wd value increased approximately 3-fold (from
11 to 30); these data also tracked with the simulated Mc (red curve, Figure c), as swelling theory would predict.[57] Similarly, a more detailed treatment taking ϕ0 and ϕ into account provided even better agreement between
the experimental and simulated results (see Figure S17 in Section G of Supporting Information). Optical images of the parent and daughter gels (Figure d) show that increased monomer
conversion leads to progressively larger daughter gels; PRCG enables
macroscopic gel growth.To verify that PRCG is a living process,
we conducted gel disassembly
studies to analyze the molecular weight and dispersity of the parent
and daughter network strands. The experimental design for this procedure
is outlined in Figure a. Aminolysis of the TTC groups in the parent gel I via exposure
to excess piperidine yields soluble 11.3 kDa star polymers, as expected
given the mass of Tetra-DBCO-PEG (Figure b). Analogous aminolysis of four daughter
gels prepared via PRCG for 1–4 h also yielded star polymer
products; these products reflected the original mass of the Tetra-DBCO-PEG
plus the newly grown polyNIPAAM (Figure b). Consistent with a living process, the
molar masses of these disassembly products progressively increased
with irradiation time; the dispersity indices stayed relatively low
(≤1.35), and there was no significant low molecular weight
tailing. A high molecular weight shoulder was observed in each case,
including for the parent gel (labeled with * in Figure b), which we attribute to disulfide bond
formation between the thiol-terminated star polymer disassembly products.
Nevertheless, these data represent an enormous improvement over the
poorly controlled UV-induced process we reported previously;[31] these are, to our knowledge, the first examples
of living additive manufacturing via a photocontrolled process.
Figure 4
Network disassembly
studies to verify the controlled nature of
PRCG. (a) Aminolysis of parent gel I and PRCG-produced
daughter gels yields star polymer products. Strand growth in the daughter
gels is reflected in the mass of the star polymer disassembly products.
(b) GPC traces for parent (black) and daughter gels prepared after
PRCG for 1–4 h. Note: aminolysis produces star polymers with
thiol chain ends. Due to a small amount of disulfide bond formation
between these products, a high molecular weight shoulder is typically
observed (labeled with * on the parent gel GPC trace) in these samples.
Network disassembly
studies to verify the controlled nature of
PRCG. (a) Aminolysis of parent gel I and PRCG-produced
daughter gels yields star polymer products. Strand growth in the daughter
gels is reflected in the mass of the star polymer disassembly products.
(b) GPC traces for parent (black) and daughter gels prepared after
PRCG for 1–4 h. Note: aminolysis produces star polymers with
thiol chain ends. Due to a small amount of disulfide bond formation
between these products, a high molecular weight shoulder is typically
observed (labeled with * on the parent gel GPC trace) in these samples.
Living Insertion of Various
Monomers and Cross-linkers into
TTC-Containing Parent Polymer Networks via PRCG
Having demonstrated
that PRCG can facilitate living additive manufacturing of daughter
gels via controlled insertion of NIPAAM we sought to further control
the daughter network structure and properties by combined addition
of monomers and cross-linkers. In the studies described above (Figure ), network growth
occurred concomitantly with a softening of the material. We envisioned
that through the use of mixtures of M and CL, chain extension could
be offset by the introduction of new cross-links to enable decoupling
of the network composition from mechanics (Figure a). In this approach, daughter gels with
novel compositions and precise cross-linking densities, and therefore
tunable mechanical properties, could be produced from the same parent
gel.
Figure 5
Living additive manufacturing via PRCG with monomers and cross-linker.
(a) Schematic for PRCG in the presence of monomer and cross-linker.
(b) The storage modulus of gel samples as a function of the cross-linker/monomer
ratio. (c) Weight ratios of gel samples (blue curve) swollen in pure
H2O (Ww) and at dry state (Wd), and simulated average chain length between
network junctions (red curve) as a function of the cross-linker/monomer
molar ratio. (d) Optical images of gel samples (III-a to III-f) swollen in pure water. (e) Images showing
the simulated networks before (top) and after (bottom) PRCG in the
presence of monomer and cross-linker (unreacted beads are not shown
for visual clarity). (f) The storage moduli (blue curve) and weight
ratios of gel samples (red curve) swollen in pure H2O (Ww) and in the dry state (Wd) as a function of the PNIPAAM weight fraction in dry gels.
(g) The effect of the cross-linker/monomer molar ratio on the storage
moduli of gels produced using two different monomers. Red curve: M
= BA, CL = neopentyl glycol diacrylate, swollen in DMF at 20 °C;
Blue curve: M = PEGMEA, CL = neopentyl glycol diacrylate, swollen
in pure water at 20 °C.
Living additive manufacturing via PRCG with monomers and cross-linker.
(a) Schematic for PRCG in the presence of monomer and cross-linker.
(b) The storage modulus of gel samples as a function of the cross-linker/monomer
ratio. (c) Weight ratios of gel samples (blue curve) swollen in pure
H2O (Ww) and at dry state (Wd), and simulated average chain length between
network junctions (red curve) as a function of the cross-linker/monomer
molar ratio. (d) Optical images of gel samples (III-a to III-f) swollen in pure water. (e) Images showing
the simulated networks before (top) and after (bottom) PRCG in the
presence of monomer and cross-linker (unreacted beads are not shown
for visual clarity). (f) The storage moduli (blue curve) and weight
ratios of gel samples (red curve) swollen in pure H2O (Ww) and in the dry state (Wd) as a function of the PNIPAAM weight fraction in dry gels.
(g) The effect of the cross-linker/monomer molar ratio on the storage
moduli of gels produced using two different monomers. Red curve: M
= BA, CL = neopentyl glycol diacrylate, swollen in DMF at 20 °C;
Blue curve: M = PEGMEA, CL = neopentyl glycol diacrylate, swollen
in pure water at 20 °C.To demonstrate this concept, PRCG was used to prepare a series
of daughter gels (III-a to III-f) from the parent gel I via insertion of bis-acrylamide cross-linker and NIPAAM
in various ratios (method B, see Section E in Supporting Information; note: vinyl conversion was held constant
at 70% for each daughter sample as measured by 1H NMR). G′ values were measured for each daughter hydrogel.
As shown in Figure b, when the molar ratio of cross-linker to monomer increased from
0.1% to 5.0%, G′ varied from 1400 to 23100
Pa, respectively. Keeping in mind that parent gel I has
a modulus of 4400 Pa (Figure b), these data show that it is possible to produce softer
or stiffer daughter gels, each with the same NIPAAM content, by simply modulating the monomer to cross-linker ratio. The waterswelling ratios (Ww/Wd) of gels from III-a to III-f were measured. As shown in Figure c (blue curve), a higher molar ratio of cross-linker/monomer
led to a lower Ww/Wd value, indicating a smaller mesh size for the corresponding
daughter gel. According to simulation results (Figure c, red curve), the molar ratio of cross-linker/monomer
indeed has a profound effect on the average Mc, which follows the same trend as the experimental Ww/Wd values.[59] Since Mc and Ww/Wd both describe
the mesh size of polymer networks (see Figure S17 for a more detailed treatment), the consistency of the
simulation and experimental results suggests that the PRCG process
follows the kinetics of living polymerization. Optical images (Figure d) show the size
of the swollen daughter hydrogels (III-a to III-f) as a function of the amount of cross-linker added. Here again,
each material has the same overall monomer composition, but differences
in cross-linking density lead to dramatically different swelling ratios.Notably, among the six daughter gel samples prepared, III-c (cross-linker/monomer ratio = 0.5%) had the same G′ and swelling ratio, within error, as the parent gel I. In other words, compared to gel I, . The case of III-c highlights a key advantage of living
PRCG: though there are many examples of generating softer or stiffer
gels using light, to our knowledge, no other methods could accomplish
this outcome of uniform network growth with no change in modulus.
Practical implementation of PRCG will benefit from this ability to
grow new materials without compromising their mechanical properties.As for all of the samples in Figure b–d, daughter gel III-c was formed
at 70% vinyl conversion. Simulations (Figure e and Figure S15) suggested that the monomers and cross-linkers are evenly distributed
throughout the daughter network following PRCG. On the basis of these
results, we speculated that the storage modulus could be similarly
held constant between parent and daughter gels if the same cross-linker/monomer
ratio was used as for III-c (0.5%) but at different vinyl
conversion values. To test this concept, three new daughter gels (IV-a to IV-c) were produced with 0.5% cross-linker/monomer
at different values of vinyl conversion (see section E-5 in Supporting Information for details). As shown
in Figure f, G′ and Ww/Wd values for these materials were similar to those of
gel I. Thus, though these materials have different compositions
their mechanical properties are very similar. The 0.5% cross-linker/monomer
ratio appears in this case to be generally applicable for achieving
uniform daughter gel growth with minimal impact on mechanics.Having demonstrated living additive manufacturing via PRCG with
NIPAAM monomer and cross-linkers, we next studied the monomer scope
of this system by replacement of NIPAAM with other monomers. A series
of daughter gels with varying cross-linker/monomer ratios were first
prepared where NIPAAM was replaced with the hydrophobic monomer n-butyl acrylate (BA). In contrast to the NIPAAM materials
described above, these BA-modified daughter gels collapsed in water
but swelled in DMF, reflecting the difference in polarity of BA compared
to NIPAAM. The G′ values for DMF-swollen BA-gels
ranged from 1400 to 13300 Pa depending on the amount of CL used (Figure g). Similarly, hydrophilic
poly(ethylene glycol) methyl ether acrylate (PEGMEA) monomer was used
in place of NIPAAM, which resulted in water-swellable daughter hydrogels
with G′ values varying between 2700 and 13700
Pa depending on the amount of CL used (Figure g). For both BA and PEGMEA monomers, by using
the correct cross-linker/monomer ratio and varying the irradiation
time (i.e., vinyl conversion), it was possible to fabricate a series
of daughter gels that differed in size and composition but had the
same G′ as the parent gel I.
Collectively, these results demonstrate that PRCG is a general strategy
to achieve living additive manufacturing of daughter gels with a range
of mechanical strengths and chemical compositions where these two
factors are decoupled via the use of cross-linker and monomer mixtures.
Living Additive Manufacturing of Stimuli-Responsive “Smart”
Materials via PRCG
Next, we investigated the use of living
additive manufacturing via PRCG to generate daughter gels with stimuli
responsive properties that were not present in the parent gel. The
lower critical solution temperature (LCST) behavior of polyNIPAAM
in water is well-known;[60] we reasoned that
daughter gels produced via insertion of different amounts of NIPAAM
should display varied LCST behaviors compared to the parent PEG gel I. To demonstrate this concept, we first measured the temperature
dependence of the storage moduli of gel I and NIPAAM-inserted
daughter gels IV-a to IV-c. As shown in Figure a, while the G′ value of the parent network I did
not change significantly in the temperature range from 20 to 50 °C,
the storage moduli of daughter gels IV-a to IV-c, with increasing mass fractions of PNIPAAM, began to increase at
∼25 °C and plateaued at higher temperatures to final values
that were 2.1, 6.0, and 9.1 times, respectively, their initial values
at 20 °C. These data indicate that the degree of increase in G′ above LCST is closely related to the mass fraction
of NIPAAM in the materials, a well-known phenomenon in other NIPAAM
copolymer materials.[61−64] We also investigated the temperature dependence of the equilibrium
swelling ratios of these samples (Figure b). When the temperature was gradually raised
above the LCST, the changes in the swelling ratios became increasingly
greater (V20/V50 = 1.6, 2.4, and 3.9, respectively) as the mass fraction of NIPAAM
increased from IV-a to IV-c. Optical images
provided in Figure c clearly show the volume changes of the daughter gels upon changing
the temperature from 20 to 50 °C. Sample IV-c, which
has the most NIPAAM, not only shows a large volume change, but also
a shift from transparent to opaque. These transformations are fully
reversible, which suggests that living additive manufacturing via
PRCG could offer a versatile strategy for the fabrication of complex
thermally responsive mechanical or optical gel actuators.[65]
Figure 6
Daughter gels with variable properties by PRCG insertion
of new
monomers into the parent gel I. (a and b) For daughter samples IV-a to IV-c, mass fractions of NIPAAM are increasing,
see Figure F. (a)
Temperature dependence of the storage modulus of parent gel I and daughter gels IV-a to IV-c. (b) Temperature dependence of the equilibrium swelling volume ratios
of parent gel I and daughter gels IV-a to IV-c, in which VT and V50 are the equilibrium volumes of hydrogels
at T and 50 °C, respectively. (c) Optical images
of the hydrogel samples I and IV-a to IV-c in the swollen state at 20 °C (LCST) in pure water. (d) Storage
moduli (blue curve) for daughter gels V-a to V-d (swollen in DMF) and their weight ratios (red curve) in DMF and
water as a function of the weight fraction of PBA in dry gels. (e)
Optical images of daughter gel samples V-a to V-d swollen in DMF and collapsed in pure water, both at 20 °C.
Daughter gels with variable properties by PRCG insertion
of new
monomers into the parent gel I. (a and b) For daughter samples IV-a to IV-c, mass fractions of NIPAAM are increasing,
see Figure F. (a)
Temperature dependence of the storage modulus of parent gel I and daughter gels IV-a to IV-c. (b) Temperature dependence of the equilibrium swelling volume ratios
of parent gel I and daughter gels IV-a to IV-c, in which VT and V50 are the equilibrium volumes of hydrogels
at T and 50 °C, respectively. (c) Optical images
of the hydrogel samples I and IV-a to IV-c in the swollen state at 20 °C (LCST) in pure water. (d) Storage
moduli (blue curve) for daughter gels V-a to V-d (swollen in DMF) and their weight ratios (red curve) in DMF and
water as a function of the weight fraction of PBA in dry gels. (e)
Optical images of daughter gel samples V-a to V-d swollen in DMF and collapsed in pure water, both at 20 °C.Next, we envisioned that by tuning
the conversion of BA within
daughter gels a series of hydrophobic gels with the same storage moduli
in organic solvent (DMF), but different swelling behaviors in water,
could be prepared from the parent gel I. Samples V-a to V-c, which contained increased mass fractions
of PBA (10%, 49%, and 65%, respectively), were prepared from gel I using a mixture of BA and 0.7 mol % CL. G′ values for this series of gels swollen in DMF were fairly
consistent (Figure d, blue curve), indicating that if the proper ratio of CL/monomer
is chosen, the stiffness of the daughter gels can be maintained during
the course of PRCG. However, as also shown in Figure d (red curve), the weight ratios (WDMF/WH2O) of these
samples when swollen in DMF or water at 20 °C gradually increased
from 2.1 to 6.7 as the percentage of BA increased. In particular,
when 90% BA was incorporated (sample V-d see and Section
E-6 in Supporting Information), a weight
ratio (WDMF/WH2O) as high as 8.3 was observed. These differences in daughter gel
volume in DMF versus water can be seen in the optical images provided
in Figure e; when
daughter gel V-d was moved from DMF to water, it not
only underwent a significant size change (Figure e, bottom right), but also experienced a
transparent-to-opaque transition as a result of the high mass fraction
of hydrophobic BA. To summarize, the incorporation of hydrophobic
BA monomer into parent gel I produces daughter gels with
completely changed solubility properties and yet a constant stiffness
in organic solvents, a feat that would be impossible using existing
nonliving polymerization techniques.
Healing and Welding Daughter
Gels with PRCG
Having
demonstrated that PRCG provides a straightforward approach to simultaneously
regulate the mechanical properties and chemical compositions of gels,
we sought to investigate further its potential in a range of gel fabrication
and modification applications. Given that these networks are built
from dynamic covalent TTC groups, we expected that they should be
able to undergo photoinduced healing when damaged.[26,30] First, we examined the healing behavior of the parent PEG-TTC gel I under blue LED light in the presence of PTH but absence
of monomer or cross-linker. As shown in Figure a, when a severely cut sample (gel I was cut in a cross direction) was directly irradiated with
blue LED light for 4 h, the resulting gel still had visible nicks
where it was cut; healing in the absence of additional monomer or
cross-linker was not effective in this system. In contrast, if the
damaged gel was first treated with a solution containing NIPAAM, bis-acrylamide,
and PTH, and then exposed to blue LED light for 4 h, a healed gel
with no visible damage was obtained. Tensile testing experiments (Figure b) revealed that
the tensile modulus and toughness of the healed material were not
decreased relative to those of the precut parent gel I. In the low strain region, the stress–strain curves for gel I and the healed sample had similar slopes; the precut and
healed materials had similar tensile moduli. The healed gel displayed
enhanced toughness (from 6 ± 1 J·m3 to 13 ±
3 J·m3; see Supporting Information Section H), which could be ascribed to the introduction of new cross-links
at the severed interface during the PRCG healing process.
Figure 7
Applying PRCG
as a versatile tool for gel healing, welding, and
smart material fabrication. (a) Optical images of damaged hydrogel I after exposure to blue LED light in the absence and presence
of monomer, cross-linker, and PTH. (b) Tensile response stress–strain
curves for gel I and a gel sample after VLPH-induced healing. (c and
d) Optical images illustrating photogrowth induced welding of two
separated gels. (e–g) Optical images showing smart materials
with site-specific stimuli-responsiveness properties produced by VLPG.
(e) Appearance change from a disk-shaped gel to a “bow-tie”
like gel. (f) Appearance change from a disk-shaped gel to an “over
easy” like gel. (g) Appearance changes of a “mouse”
like gel.
Applying PRCG
as a versatile tool for gel healing, welding, and
smart material fabrication. (a) Optical images of damaged hydrogel I after exposure to blue LED light in the absence and presence
of monomer, cross-linker, and PTH. (b) Tensile response stress–strain
curves for gel I and a gel sample after VLPH-induced healing. (c and
d) Optical images illustrating photogrowth induced welding of two
separated gels. (e–g) Optical images showing smart materials
with site-specific stimuli-responsiveness properties produced by VLPG.
(e) Appearance change from a disk-shaped gel to a “bow-tie”
like gel. (f) Appearance change from a disk-shaped gel to an “over
easy” like gel. (g) Appearance changes of a “mouse”
like gel.Given that it is possible to heal
severed gels via PRCG, it should
also be possible to weld together independently synthesized parent
and/or daughter gels to produce new complex gel progeny with distinct
spatially differentiated compositions. To demonstrate this welding
process, we prepared two identical parent gel I samples,
each containing monomer, cross-linker, and PTH. These parent gels
were then placed in direct contact in either a “face to face”
or “shoulder to shoulder” orientation and exposed to
blue LED light. As shown in Figure c and Figure d, PRCG led to a robust fusion of the two parent gels; the
welded gels could be repeatedly bent to up to 90° without fracture.Finally, sincePRCG offers a convenient strategy for modifying the
composition and mechanics of gels, and the capability of controlling
polymerization both spatially and temporally using light, we reasoned
that it should be possible to use this method to fabricate spatially
responsive materials. To demonstrate this concept, three new progeny
gels (Figure e,g)
were prepared from the same parent gel I using a series
of PRCG processes (see section H-3 in Supporting Information for details); here again, such a feat would be
impossible without the living nature of PRCG, which enables repeatable
reactivation of the network strands multiple times to achieve successive
growth and welding events. In Figure e, two NIPAAM-containing daughter gels were welded
together with two PBA-containing daughter gels. When this complex
progeny gel was swollen in organic solvents (i.e., MeCN), where all
domains are swollen, a disk-shaped gel material was afforded (Figure e, far left). Immersing
the material in water at 20 °C led to collapse of the PBA components,
resulting in an oval-shaped gel (Figure e, center). When the water temperature was
raised to 50 °C (above the LCST of polyNIPAAM), the polyNIPAAM
components of the material collapsed and become opaque (Figure e, right), producing a “bow-tie”
like appearance. In another example (Figure f), a ring-shaped daughter gel and a round
daughter gel, each containing different mass fractions of NIPAAM,
were prepared separately via PRCG and then welded together via PRCG
to produce a complex progeny material with varied NIPAAM content.
This material appeared uniform when swollen in water at 20 °C;
raising the temperature above LCST led to an “over easy egg”
appearance due to the transparent-to-opaque transition in the outer
ring, which contained a higher NIPAAM mass fraction. In the last example
(Figure g), a “mouse”
like progeny gel was prepared by PRCG welding together three different
daughter gels each prepared by PRCG: one with a PEGMEA (“face”),
one with NIPAAM (“left ear”), and one with BA (“right
ear”). In organic solvent (MeCN), the “mouse”
gel had symmetric features. In contrast, its “right ear”
shrank upon exposure to water, while its “left ear”
shrank upon heating above the LCST of polyNIPAAM. To our knowledge,
these are the first examples of multistep living additive manufacturing
to produce complex spatially patterned gel materials.
Conclusion
To conclude, we have developed a first-generation living additive
manufacturing process called PRCG that enables the controlled insertion
of monomers and cross-linkers into polymer networks to produce complex
daughter objects from a single type of parent object. PRCG makes use
of a newly developed photoredox catalyzed polymerization that avoids
the undesired chain termination processes that are present in traditional
free radical and iniferter polymerizations. Our approach enabled the
fabrication of daughter gels with complex compositions and mechanical
properties that would be difficult or impossible to achieve using
traditional free radical polymerization methods. In particular, we
demonstrated that with the proper cross-linker to monomer ratio, we
could grow daughter gels to different dimensions with new network
compositions and yet with unmodified mechanical properties; material
composition and mechanics were decoupled. Excellent agreements between
experimental and simulated PRCG results provided a firm rationale
for the observed changes in gel properties that is based on the living
increase of Mc and uniform changes in
cross-linking density. It should be noted that this proof-of-concept
work only hints at the potential of living additive manufacturing
via PRCG as a tool for the synthesis of complex materials. For practical
applications, PRCG will require extensive development: the polymerization
rate should be increased by at least an order of magnitude, the oxygen
tolerance should be thoroughly investigated,[42] and the expansion to bulk polymeric materials should be pursued;
these studies are ongoing in our laboratory. Furthermore, one could
imagine using traditional additive manufacturing devices to produce
TTC-based networks suitable for subsequent living additive manufacturing
modifications; the two approaches could work in concert to enable
unprecedented material functions. We believe that these results represent
an important first step in the development of living additive manufacturing.
Methods
See Supporting Information for full
descriptions of all methods, characterization data, experiments, and
simulations.
Synthesis of Parent Gel I and Representative Living
Additive Manufacturing via PRCG Experiment
An oven-dried
vial (1.8 mL) was charged with a solution (50 μL) of tetra-DBCO-PEG
(15.0 mM), monomer, PTH (0.03 mol % of monomer) without cross-linker
(method A) and with cross-linker (method B) in acetonitrile (MeCN)
in a glovebox. A solution (50 μL) of bis-N3-TTC (30.0
mM) in MeCN was added in one portion into the vessel. The solution
was vortexed to afford sufficient mixing. Gelation was observed within
10 min. The reaction was kept in the dark for 24 h to ensure maximal
conversion. Then, the vessel was taken out from the glovebox and exposed
to LED light irradiation in a cold room (4 °C) for the desired
time. After the reaction, the gel was removed from the vessel and
swollen in MeCN at room temperature. The MeCN solvent was exchanged
for at least five times to completely extract unreacted NIPAAM from
the gel. The collected organic solution was concentrated under a vacuum.
Butyl benzoate was added into the mixture as an internal standard
in the 1H NMR experiment for the calculation of monomer
conversion. MeCN was then removed to give a dry gel. The material
was weighed to afford a dry weight (Wd). Then, the dry gel was fully swollen in pure water at room temperature.
The swollen weight (Ww) and modulus (G′) were measured for this hydrogel. Swelling ratios
were defined as the value of Ww/Wd. At least three gels were prepared and tested
to obtain each data point.
Authors: Jeremiah A Johnson; Jeremy M Baskin; Carolyn R Bertozzi; Jeffrey T Koberstein; Nicholas J Turro Journal: Chem Commun (Camb) Date: 2008-04-24 Impact factor: 6.222
Authors: Jordan C Theriot; Chern-Hooi Lim; Haishen Yang; Matthew D Ryan; Charles B Musgrave; Garret M Miyake Journal: Science Date: 2016-03-31 Impact factor: 47.728
Authors: Matthew D Ryan; Jordan C Theriot; Chern-Hooi Lim; Haishen Yang; Andrew Lockwood; Nathaniel G Garrison; Sarah R Lincoln; Charles B Musgrave; Garret M Miyake Journal: J Polym Sci A Polym Chem Date: 2017-03-16 Impact factor: 2.702
Authors: Kaihuan Zhang; Wenqing Yan; Rok Simic; Edmondo M Benetti; Nicholas D Spencer Journal: ACS Appl Mater Interfaces Date: 2020-01-24 Impact factor: 9.229