3.1. Polymerization Rate
The kinetics of polymerization of the cationic monomers for the synthesis of AB diblock copolymers can be described by a pseudo-first-order reaction [
13] according to
where [
B]
0 is the initial monomer concentration, [
B] is the monomer concentration,
k is the polymerization rate constant, and
t is the time. To determine the effect of chemical feedback on the polymerization rate in the templated reaction when the concentration of monomers, the length of the neutral block, and other parameters vary, we compare with the respective polymerization rate of the non-templated polymerization, in which there is no assembly, and hence, no chemical feedback. To investigate the influence of concentration on chemical feedback, simulations of mixtures containing 500 neutral homopolymer chains A
50, 10000 positively charged B type monomers, 1500 initiator beads, and 10000 counterions were performed. For the templated polymerization, 500 additional templates C
20 and 10000 counterions were considered. The reaction probability was set to 0.125. Using different simulation box sizes, concentrations of [
Φ]=0.04, 0.12, 0.24 and 0.36 were achieved. The target length of the polymerized positively charged block of the copolymer was set to 20 beads (A
51B
20). The kinetic plots obtained from the simulation are illustrated in
Figure 3. The resulting polymerization rate constants are presented in Table S2.
As can be observed the polymerization rate in the templated reaction at [
Φ]=0.04 is much faster than in the non-templated polymerization (
Figure 3a,c). This is in full agreement with the experimental results of Bos et al. [
13] reported for similar concentrations. The increase to [
Φ]=0.12 increases both the reaction rates. However, the ratio of the rates of the two polymerization types becomes much smaller. Furter increase to [
Φ]=0.24 and 0.36 (
Figure 3b,c) leads to the opposite result, i.e., the non-templated polymerization rate becomes higher than the templated polymerization. This is in full agreement with the experimental results by Ding et al. [
14] for concentrations of 16% and 50% w/w (coacervate in water). Since the reaction probability in the simulations is constant in both cases, the local monomer concentration before the polymerization takes place may is clear measure of the complex dependency of the polymerization rate on the concentration. To quantify the local monomer concentration in the templated polymerization, the radial distribution functions
g(
rCB) of the template and the monomer beads were calculated from 200 simulation snapshots obtained by a trajectory of one million timesteps after the initial equilibration (
Figure 4). Three independent simulations of the mixture with [
Φ]=0.36 each one starting from a different initial configuration were used for the calculation of the standard deviation of
g(
rCB). The integration of
g(
rCB) up to a radius of ca. 3.5σ yields the number of B type beads that surround each C type bead. From this number the local concentration of monomers within the spherical volume with this radius can be computed. For the non-templated polymerization, the calculation of local concentration of monomers is straightforward, since the system is homogenous without template beads, and equals to the total monomer density in the simulation box.
As shown in
Figure 5 and Table S2, the ratio of local monomer concentrations of the templated to the non-templated polymerizations decreases with the total concentration in a similar way as the ratio of polymerization rate constants decreases with [
Φ] (
Figure 3c). This shows that the local concentration may is the key parameter for understanding the variation of polymerization rate with the concentration. At [
Φ]=0.04, the local concentration of the monomers around the template is two times the respective of the non-templated solution accelerating this way the templated polymerization. The difference in local monomer concentrations for the two types of polymerizations decreases at [
Φ]=0.12. Nevertheless, the local monomer density in the templated polymerization is always higher, leading in a higher polymerization rate. At the most concentrated systems ([
Φ]=0.24 and 0.36), the LJ interactions have a strong impact on the templated polymerization rate. The repulsion between the template, and the monomers prevents them from coming close, and thus, both the local density and the polymerization rate in the templated reaction become smaller than in the non-templated reaction.
To study the effect of LJ interactions, separate simulations with the LJ interaction parameters set to
εBC=1,
εBB=1.5, and
εCC=1.5, at
T*=3.0 were performed at [
Φ]=0.24. In this way, the B-B and C-C type interactions remain in bad solvent conditions as previously, but the B-C interactions correspond to theta solvent for the neutral chains [
9]. As shown in
Figure 6, the templated polymerization rate becomes much higher than in the non-templated case since both the neutralized template and the monomers prefer to be close to each other, increasing this way, the local concentration around the template.
To study the effect of the template length on the polymerization rate, simulations of mixtures of 500 A
50 neutral chains and a varying number (i.e., 500, 250, 125 and 80) of template chains consisting of 20, 40, 80 and 125 C type beads, respectively, were performed at [
Φ]=0.24. The target length of the copolymer chains was set to A
51B
20. B-B and C-C interactions are kept attractive, corresponding to bad solvent conditions (
T*=2.0), while all other interactions are considered repulsive. As shown in
Figure 7 the polymerization rate increases non-linearly with the increase of template length. In the mixtures with the longest template C
125, the polymerization rate approaches the rate of non-templated polymerization, which is in general higher for [
Φ]>0.18. Long template chains may conform to an elongated shape which favors the attractions with the oppositely charged monomers. This increases the monomer local concentration and the polymerization rate.
The effects of chemical feedback on the polymerization rate when the neutral chain length varies from 25 to 50 and 100 A type beads for both templated and non-templated reactions are studied for the lowest concentration ([Φ]=0.04). In all cases, the target length of the B type block for the copolymers was fixed, i.e., A26B20, A51B20 and A101B20.
As shown in
Figure 8, both the templated and the non-templated polymerization, the increase in the length of the neutral block leads to the linear decrease of the polymerization rate. This is because the excluded volume interactions between the A and B hinder monomers from approaching the active B type end beads (reduced monomer concentration around the active centers). The decrease in the non-templated polymerization rate is enhanced compared to the templated polymerization. As discussed earlier, in the templated polymerization a lot of monomers are stuck on the template, even before the polymerization starts. Thus, the excluded volume interactions with the A type blocks concern a smaller number of free monomers. In contrast, in homogeneous non-templated polymerization, all monomers experience excluded volume interactions with A type blocks. This hinders monomers from approaching the active end beads.
3.2. Molecular Weights and Polydispersity
The mass distributions of the B block of the A
51B
20 copolymers obtained from both types of polymerizations are presented in
Figure 9 for [
Φ]=0.04, 0.12, and 0.24. A C
20 template is used and RP is set to 0.125. From these distributions, the number (
Mn) and weight (
Mw) average molecular weights, and the polydispersity index (PDI=
Mw/
Mn) can be calculated. The results are listed in Table S1 in the Supporting Information. From the simulations, we have verified that copolymer chains consisting of one or two B type beads (i.e., A
51B
1, A
51B
2) do not participate in the micellization. Thus, these copolymers are considered as impurities and are not counted in the calculation of
Mw,
Mn and PDI. As can be seen in Table S1, the
Mn,
Mw and PDI of the B type block obtained from the templated polymerization are higher than the respective quantities in the non-templated polymerization, especially at low and moderate concentrations [
Φ]=0.04 and 0.12. This is because in the templated polymerization where half of the monomers are lying on the oppositely charged templates, many neutral chains remain without or with only 1 or 2 B type beads. In the non-templated polymerization, where the monomers are homogeneously distributed in the solution, almost all A type chains participate in the polymerization. In this case, the chains have narrow molecular weights and low PDI. Experimental results of the PDI values of the whole diblock copolymer chains (PDI
diblock) and the pre-synthesized A type precursors (PDI
B) are reported [
14]. To extract PDI
B and to compare with the simulation results, the following equation is used [
33]
where
wA and
wB are the ratios of the number of beads of the A and B block to the total number of beads in the diblock copolymer, respectively.
Figure 10a and 10d show the PDI
B and
Mw as a function of [
Φ], respectively. As can be observed, in the templated polymerization, the increase in the concentration decreases both the PDI
B and
Mw. In the non-templated homogeneous polymerization, the trend is the opposite; Both PDI
B and
Mw increases with [
Φ]. At [
Φ]=0.24, the difference between the PDI
B values for the two types of polymerizations become very small. Using the experimental values (
=1.10 and
=1.2) of Ding et al. [
14], which are the same for both types of polymerizations at [
Φ]=0.5 in Equation (2), we predicted the
=1.2. This value is close to the simulation mean value of 1.26 at [
Φ]=0.24.
Our simulation results show that the difference in the PDI
B values between templated and non-templated polymerization at [
Φ]=0.04 is significant in full agrement with the simulation results of Gavrilov et. al. [
15] for PISA polymerization. They found that the polydisperity of the diblock copolymer varies from 1.07 to 2.15 as the strength of the interactions between moieties is changed. However, no direct comparison with the experimental results can be done, since Bos et al. [
13] do not report the PDI
B values for the non-templated polymerization. PDI and
Mw as functions of the A type block length are presented in
Figure 10b, and e respectively, for [
Φ]=0.04. It can be seen that the increase from A
26 to A
51 leads to a decrease in PDI. This is because the longer neutral chain covers the active end bead of the polymerized B block preventing the monomers to approch. The effect of RP on PDI and
Mw are presented in
Figure 10c,f for [
Φ]=0.04. In the non-templated polymerization, the increase of the RP from 0.125 to 0.25 leads to the increase of
Mw and PDI values. However, further increase to 0.5 has no extra effect on them because the local concentration of monomers around the active polymerization center cannot further increase.
3.3. Micelle Size and Shape
The effects of the chemical feedback on the size and shape of the micelles were studied at the lowest concentrations, i.e., [
Φ]=0.04. The simulations of the PIESA one-step micellization were performed for the following mixtures: (a) A
25 + C
20, (b) A
50 + C
20, and (c) A
100 + C
20. The target diblock copolymers were A
26B
20, A
51B
20, and A
101B
20, respectively. To model the two-step micellization, after the end of polymerization, the C
20 templates were added to the simulation box. The simulation scheme is described in detail in the model section. The mass distribution functions of the micelles computed from the molecular dynamics trajectories using the new python code are shown in
Figure 11 as a function of the aggregation number
N.
Figure 11 clearly shows that in the templated polymerization micelles with higher aggregatiom numbers are formed. Regardless of the micellization method, the increase of the neutral block in the diblock copolymers from A
26B
20 to A
51B
20 and further to A
101B
20 leads to smaller aggregates. This is expected because the increase in the hydrophilic block makes the corona of the micelle bulkier, better protecing the hydrophobic core formed by the complexation of the oppositely charged B and C beads. However, the mass distibution profiles obtained from the PIESA differ significantly from the two-step micellization. In PIESA the mass distribution profile is a Gaussian- like function (micelles with preferential aggregatiom number are formed as shown in
Figure 11b). The deviations from the Gaussian function
Figure 11a,c can be attributted to the difficulties in the equilibration arising from the smaller neutral block and the higher
Mw of PIESA chains respectively. In sharp contrast, the mass distribution profiles obtained from the two-step micellization do not reveal preferential aggregation [
9] (decaying function with
N,
Figure 11d–f). The evolution of micelle mass distribution with the time in the templated polymerimerization is presented in Figure S2 for the mixture of A
51B
20 + C
20. Initially small micelles are formed then progresivelly the aggregation number of micelles is increasing and after completion of the polymerization the size reareangements leads in the gaussian type distribution presented in
Figure 11b. Snapshots of the simulation box are presented in Figure S3 for the same mixture at concentrations [
Φ]= 0.04 and 0.36 and different simulation times
τ.
The mean squared radii of gyration <
S2>
PIESA and <
S2>
two-step, describing the size of the micelles for the PIESA and the two-step micellization, respectively, are shown in
Figure 12 as a function of the aggregation number. <
S2>
two-step is always higher than <
S2>
PIESA. This finding is in full
aggrement with the experimental results of Bos et. al. [
13]. The deviation between <
S2>
two-step and <
S2>
PIESA decreases as the length of the neutral block forming the corona becomes much larger than the B type block (
Figure 12b,c). The lower values of <
S2>
PIESA may be due to the higher PDI
B which is 1.3 for PIESA, compared to 1.1 for the two-step micellization. Van der Kooij et. al. [
3] and Gavrilov et. al. [
15] have shown that the diblock copolymer chains with higher PDI resulted in denser packing in the micelle core. Thus, the overall mean squared radius of gyration value of the polyelectrolyte complex micelles was much lower than the respective of micelles formed by the low PDI copolymers. The shape anisotropy parameter [
9,
20]
κ2 (
Equation (S2) in the Supporting Information) is shown in
Figure 13 as a function of the aggregation number of the micelles for the two micellization schemes. From
Figure 13, it is evident that micelles with very small aggregatiom numbers (
N<10) are elongated (
κ2 > 0.1). The micelles are shperical (
κ2 < 0.1) at moderate aggregation numbers, and again elongated for higher aggreegation numbers (
N>90). The
κ2 values for micelles with high aggregation numbers are scattered since this calculation suffer from bad statistics because such big micelles rarely form in the simulation. In general, micelles with aggregation numbers 20<
N <80 formed by the PIESA micellization are more spherical than the ones in the two-step micellization for the A
26B
20 + C
20, and A
51B
20 + C
20 mixtures. In contrast, the micelles obtained from the A
101B
20 + C
20 mixture (i.e., the system with the longest neutral A type block) have similar shape in both micellization schemes. The reason is that the shape of the large corona consisting of the A
101 blocks predominaly determines the overall shape of the micelles.
So far in this study, we have focused on micelles formed by mixtures in which the ratio of the charged template beads to the oppositely carged monomers is 1:1. To study the effect of chemical feedback in mixtures with an excess of templated negative beads, simulations are performed for a 2:1 ratio. The mass distributions of the micelles obtained from A
101B
20 + C
40 mixtures are presented in
Figure 14 as a function of the aggregation number for both PIESA and two-step schemes. Our results show that, regardless of the micellization method, only very small aggregates are formed (
N ≤ 7). This finding is in full agreement with the experimental results of Boss et al. [
13], and also agrees with previous theoretical predictions of PCMs being formed only at approximately equal charge stoichiometries [
9].