Sebastian
Milster
abc,
Richard
Chudoba
abc,
Matej
Kanduč
ad and
Joachim
Dzubiella
*ac
aResearch Group for Simulations of Energy Materials, Helmholtz-Zentrum Berlin für Materialien und Energie, Hahn-Meitner-Platz 1, D-14109 Berlin, Germany. E-mail: joachim.dzubiella@physik.uni-freiburg.de
bInstitut für Physik, Humboldt-Universität zu Berlin, Newtonstr. 15, D-12489 Berlin, Germany
cApplied Theoretical Physics – Computational Physics, Physikalisches Institut, Albert-Ludwigs-Universität Freiburg, Hermann-Herder Str. 3, D-79104 Freiburg, Germany
dJožef Stefan Institute, Jamova 39, SI-1000, Ljubljana, Slovenia
First published on 7th March 2019
The selective solute partitioning within a polymeric network is of key importance to applications in which controlled release or uptake of solutes in a responsive hydrogel is required. In this work we investigate the impact of cross-links on solute adsorption in a swollen polymer network by means of all-atom, explicit-water molecular dynamics simulations. We focus on a representative network subunit consisting of poly(N-isopropylacrylamide) (PNIPAM) and N,N′-methylenebisacrylamide (BIS/MBA) cross-linker types. Our studied system consists of one BIS-linker with four atactic PNIPAM chains attached in a tetrahedral geometry. The adsorption of several representative solutes of different polarity in the low concentration limit at the linker region is examined. We subdivide the solute adsorption regions and distinguish between contributions stemming from polymer chains and cross-link parts. In comparison to a single polymer chain, we observe that the adsorption of the solutes to the cross-link region can significantly differ, with details depending on the specific compounds’ size and polarity. In particular, for solutes that have already a relatively large affinity to PNIPAM chains the dense cross-link region (where many-body attractions are at play) amplifies the local adsorption by an order of magnitude. We also find that the cross-link region can serve as a seed for the aggregation of mutually attractive solutes at higher solute concentrations. Utilizing the microscopic adsorption coefficients in a mean-field model of an idealized macroscopic polymer network, we extrapolate these results to the global solute partitioning in a swollen hydrogel and predict that these adsorption features may lead to non-monotonic partition ratios as a function of the cross-link density.
In the zoo of constituents, thermoresponsive hydrogels based on poly(N-isopropylacrylamide) (PNIPAM) are among the most intensively investigated systems, since their volume phase transition at about room temperature as well as a high water content promise good biocompatibility5,11 and make them convenient to handle. Pure PNIPAM was found to have the lower critical solution temperature (LCST) at roughly 304 K as reported by Heskins and Guilett in 1968.12 A frequently utilized cross-linker for PNIPAM gels, used in radical polymerization, is N,N′-methylenebisacrylamide, often abbreviated as BIS or MBA. BIS has chemical similarity to PNIPAM (compare Fig. 1), is non-degradable, has a very high reactivity, and retains PNIPAM's LCST.13–17
![]() | ||
Fig. 1 Chemical structures (top) and corresponding ball-and-stick representations (bottom) of poly(N-isopropylacrylamide) [PNIPAM] (panels a and b), and the cross-linker N,N′-methylenebisacrylamide [BIS] (panels c and d). Dashed lines represent possible bonds to neighboring PNIPAM monomers or BIS. Associated carbon atoms are referred to as the polymer backbone. PNIPAM's amide group and isopropyl group form side chains. The amide groups and BIS’ central methylene bridge are hydrophilic, potentially forming hydrogen bonds45 with the surrounding. The backbone and isopropyl group have a hydrophobic character. |
Besides these morphological properties, the degree of cross-linking influences solute uptake and partitioning. The partition ratio is the ratio of the solute concentrations inside and outside the gel and is therefore a crucial parameter controlling device functionality especially for drug delivery or catalytic systems. For the latter, for instance, metal nanoparticles inside hydrogels catalyze reactions and the effective reaction rates depend crucially on the concentration of the reactants in the permeable polymer matrix.7,8,18,19 The partition ratio may be affected by generic as well as specific cross-linker effects. The cross-linker density first of all simply changes the packing fraction and with that the overall steric exclusion by the polymer mesh.11 Furthermore, it has become clear that more complex, e.g., local attractive and/or electrostatic interactions can lead to complex and even cooperative effects in the partitioning.20–23 In particular, a ‘vertex trapping’ effect due to many-body attractions in the dense cross-link region has been reported in generic coarse-grained simulations of polymer networks.24–28 More specific chemical effects should also play a role, as indicated by all-atom molecular dynamics (MD) computer simulations of bare PNIPAM chains,29–31 peptide-like chains,32–34 these in combination with solutes with various polarity35–40 as well as by simulations revealing the influence of cross-links to polymer networks solvation and structural properties.41–44
The aim of this work is to investigate the effects of cross-linking on solute adsorption in swollen hydrogels made up of PNIPAM and BIS (below the volume phase transition temperature (VPTT)) by utilizing all-atom, explicit water MD simulations of a minimal polymer network setup. In order to do this, we consider one BIS cross-linker with four atactic PNIPAM chains restrained in a tetrahedral geometry. In our analysis, we subdivide the solute adsorption regions and systematically distinguish between contributions stemming from polymer chains and cross-linker parts. We probe solutes of various polarity, representing typical chemical compounds, in the highly diluted regime. We finally demonstrate in a simple model, how these contributions affect the global solute partitioning in large hydrogels as accessible by experiments.
We employ the OPLS-QM2 force field recently developed by Palivec et al.31 for the PNIPAM monomers. Compared to the standard OPLS-AA46 parameters, this force field features a reparametrization of the partial charges retrieved from ab initio calculations and further manual fine-tuning to reproduce the experimental LCST of PNIPAM. Due to the chemical similarity of BIS and PNIPAM, we adopt the very same partial charges for the cross-linker. These were confirmed by our own quantum mechanical calculations using the Gaussian 09 software.47 More details on the force field parameters are provided in Appendix A.
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Fig. 2 Simulation snapshots of the studied polymeric molecule, consisting of one BIS-linker and four PNIPAM chains, at T = 290 K and relative chain extension λ = 0.83 in (a) all-atom ball-and-stick representation and (b) showing only backbone and heavy BIS atoms inside the simulations box (![]() ![]() |
The corners of the tetrahedron, generated by the position restraints, are L = 2.87 nm distant to its centroid and the edge length accounts to 4.69 nm (Fig. 2b). We have chosen this size to ensure a relative chain stretch λ between 0.75 and 0.85, which is expected in swollen hydrogels.38 The relative chain stretch λ is defined as the ratio of the mean end-to-end distance and the contour length
![]() | (1) |
Generating such a setup starts by placing the BIS-linker in the center of the box, which is the centroid of the virtual tetrahedron. At each backbone binding site, indicated by dashed lines in Fig. 1, PNIPAM monomers with random tacticity are attached in a head-to-tail manner with the backbone axis pointing towards the desired coordinates of the position restraint. PNIPAM's backbone bonds are squeezed to match the size of the tetrahedron and were allowed to relax during the first steps (energy minimization and equilibration) of the simulation.
The edge lengths of the rectangular simulation box are chosen large enough (6.32 nm × 7.65 nm × 9.64 nm on average) in order to ensure that the position-restrained backbone terminals of different periodic images are separated by at least 3 nm in x- and y-, and 5 nm in z-direction (Fig. 2b). Thus, we avoid interactions between chain ends across the box boundaries and can locate a (water/solute) bulk phase in peripheral box regions.
The solutes are subsequently inserted at random positions in the simulation box, which is finally filled with more than 15000 SPC/E50 water molecules. Details are listed in Table 1.
Simulation specifications | Results | |||||||
---|---|---|---|---|---|---|---|---|
Aromatics | N solute | t sim [μs] | ρ 0 [mM] | |||||
B | Benzene | 1 | 12.6 | 3.2 ± 0.1 | 54 ± 3 | −2 ± 2 | 1.0 ± 0.1 | 7 ± 3 |
NB | Nitrobenzene | 1 | 11.9 | 2.8 ± 0.1 | 124 ± 6 | 5 ± 2 | 2.3 ± 0.2 | 10 ± 6 |
NB | Nitrobenzene | 20 | 1.1 | 28.0 ± 2.0 | 720 ± 220 | 70 ± 20 | 16.0 ± 2.0 | −140 ± 220 |
NP0 | 4-Nitrophenol | 1 | 12.3 | 2.8 ± 0.1 | 121 ± 17 | 21 ± 3 | 2.1 ± 0.2 | −2 ± 7 |
NP0 | 4-Nitrophenol | 20 | 1.2 | 42.1 ± 2.0 | 280 ± 60 | 100 ± 20 | 4.6 ± 0.5 | −40 ± 60 |
NP− | 4-Nitrophenolate | 1 | 8.4 | 2.3 ± 0.1 | 270 ± 20 | 43 ± 8 | 4.5 ± 0.4 | 10 ± 20 |
NP−/Na+ | 4-Nitrophenolate + sodium | 20 pairs | 1.1 | 63.0 ± 1.0 | 67 ± 3 | 14 ± 2 | 1.3 ± 0.1 | −11 ± 3 |
Others | ||||||||
C6 | Hexane | 1 | 11.2 | 3.3 ± 0.1 | 33 ± 5 | −2 ± 4 | 0.8 ± 0.1 | −1 ± 5 |
C4 | Butane | 1 | 7.4 | 3.4 ± 0.1 | 25 ± 2 | −1 ± 2 | 0.44 ± 0.05 | 5 ± 2 |
C1OH | Methanol | 30 | 3.5 | 107.3 ± 1.0 | −2 ± 1 | 0 ± 4 | −0.05 ± 0.05 | 1 ± 1 |
Na+/Cl− | Sodium chloride | 3 pairs | 8.4 | 11.5 ± 0.1 | −33 ± 2 | 5 ± 1 | −0.65 ± 0.02 | −6 ± 2 |
We further probe two alkanes, namely hexane (C6) and butane (C4), sodium chloride (Na+/Cl−), and methanol (C1OH). All compounds are visualized in Fig. 2c. If not stated otherwise, we insert one probe molecule into the system to analyze the infinite dilution limit. To estimate finite concentration effects of aromatic compounds we perform simulations with 20 solutes. List of solutes and the simulation setups are listed in the summary Table 1. The standard OPLS-AA46 force field was utilized except for the charged nitrophenolate NP−, for which the excess charge was distributed among the molecule due to the mesomeric effect,38 leading to higher polarity of the nitro group.
All covalent bonds of hydrogens were constrained with the LINCS58 algorithm. The cut-off distance for Lennard-Jones and short-range electrostatic interactions was set to 1.0 nm while long range electrostatics was accounted for by the Particle Mesh Ewald (PME) method with cubic interpolation and a grid spacing of 0.12 nm.59
Periodic boundary conditions in all three directions were used and the simulations were carried out under constant temperature and pressure, which were controlled by the velocity-rescale thermostat (at T = 290 K, τT = 0.1 ps) and the Berendsen barostat (at p = 1 bar, τp = 1 ps), respectively.60,61
After the initial energy minimization (steepest descent), the system was equilibrated in the NVT ensemble for 2 ns and in the NpT ensemble for another 10 ns. The integration step of the leap-frog integrator was set to 2 fs and data were collected every 10 ps. The total simulation time tsim per solute is summarized in Table 1.
For the 20 NP−/Na+ pairs, we only analyzed the nitrophenolate trajectories. In the case of the Na+/Cl− simulation, each ion type was analyzed individually. The results for sodium and chloride ions are very similar and yield the same results within the range of our precision and thus are presented for either type in Table 1.
Further, the PNIPAM monomer density distribution ρmer(r) is retrieved, which helps us to distinguish between different polymer adsorption domains (Fig. 3). The solutes' distributions are the basis for calculating the solute–polymer adsorption in our setup as detailed below. We demonstrate how the splitting of the adsorption into the chain and the cross-linker contributions is achieved and how this can be used to estimate partition ratios of an entire hydrogel.
![]() | (2) |
![]() | (3) |
Transferring this concept to our setup (Fig. 2), for which radial density profiles g(r) of the solutes (Fig. 4a and b) are measured from the COM of BIS, we define the partial adsorption Γ(r1,r2) counting excess solutes in the interval [r1,r2], reading
![]() | (4) |
Γtot = Γxlink + Γchain + Γend. | (5) |
The equilibrium bulk concentration ρ0 depends on the simulation box size and the binding affinity. It is convenient to define an infinite-dilution solute-specific adsorption coefficient that does not depend on concentration via
![]() | (6) |
Γchain = NmerΓmer | (7) |
![]() | (8) |
We now compare the adsorption of the solutes to the PNIPAM chain, listed in Table 1 and visualized in Fig. 5. The results can further be compared with the density profiles (Fig. 4a and b). We start with the examination of the rather weakly adsorbing species (Fig. 4a). Methanol is the smallest probe molecule tested and is highly soluble in water and shows a rather low binding propensity. It is in fact slightly attracted to the polymer, but this cannot compensate the volume exclusion effect of PNIPAM and thus its adsorption coefficient is of negative value. Methanol's preferential adsorption has already been reported in experiments64 and other simulations,65–68 studying primarily the cononsolvency of PNIPAM in water–methanol mixtures.
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Fig. 5 Adsorption coefficients (Γ* = Γ/ρ0) quantifying the binding affinities of different solutes to one PNIPAM monomer ![]() ![]() |
Sodium and chloride have the lowest binding affinity to the hydrogel, which has already been shown in previous simulations of isolated chains.35,38 As expected, simple well-hydrated ions are repelled from low dielectric (less polar) regions.
The two probed alkanes, butane and hexane, have very similar profiles. The bigger hexane shows slightly higher adsorption than butane owing to the larger surface area, which facilitates hydrophobic interactions with apolar groups of the polymer chains. The very same argument does not hold when comparing with benzene. Benzene has about the same size as the alkanes, but shows higher binding affinity than the larger hexane. On the molecular level, the adsorption mechanism looks similar. Benzene and hexane tend to preferentially make contact with hydrophobic parts of the polymer.
Comparing the aromatic compounds, which are roughly of equal size, we find the adsorption generally increases with the polarity of their substituents. The order according to their polarity, starting with the apolar benzene, is B → NB → NP0 → NP−, cf.Fig. 4b. All of them own a hydrophobic aromatic ring, interacting with the hydrogel described as in the benzene case. With one polar substituent for benzene, namely the nitrobenzene, the adsorption is more than doubled. This stems from additional hydrogen bonding45 between the nitro-oxygens and the polymer's amide hydrogens. The very same interaction mechanism applies to NP0 and NP−. The extra hydroxy tail in the case of nitrophenol (NP0) does not lead to a significant change of the adsorption to PNIPAM. On the one hand, the OH group can interact with the polymer's amide group and on the other hand, increases the water solubility. These two effects seem to compensate for NP0 adsorption to the chains, such that the adsorption is similar to the one for NB.
The deprotonated and hence charged NP− is the best adsorbing compound tested. The deprotonation leads to a redistribution of the electronic density, increasing the polarity of the whole molecule. The higher charging of the nitro-oxygens as well as the O− tail stabilize the contacts with PNIPAM's amide hydrogens, resulting in a roughly two times higher adsorption coefficient compared to NB and NP0.
Γxlink = Γ(0,ra) − ΓmerNmer(0,ra). | (9) |
Note that in comparison to PNIPAM monomers, BIS has two amide groups and no isopropyl groups, thus creating a more hydrophilic environment than the chains. The apolar compounds, B, C4, and C6 show a slightly negative binding affinity in the cross-link region. In contrast, see again Table 1 and Fig. 5, the solute adsorption increases with polarity, where nitro-aromatic solutes are especially attracted. Nitrobenzene shows a more than doubled adsorption to the cross-link region when compared to bare chain monomers. The NP0 and NP− adsorption per cross-linker is even tenfold higher. The binding mechanism is similar to the single chain adsorption. The numerous amide hydrogen combinations make it very probable for the nitro-oxygens to find binding partners.
As already stated for the chain adsorption, NP− has the most polar nitro group resulting in the strongest adsorption coefficients in this study. Examining the simulation trajectories, we repeatedly found NP− in the location shown in Fig. 6. One or both of the nitro-oxygens couple (forming hydrogen bonds) with two to three hydrogens from the amide groups: one from BIS and one or two from the PNIPAM monomers. Additionally, the hydrophobic isopropyl groups or the backbone of PNIPAM can contact, almost embed, the aromatic ring, enhancing the stability of such an adsorbed state. The same mechanism has been observed for NB and NP0, but the higher partial charges of NP− promote the binding.
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Fig. 6 Simulation snapshot of NP− (illuminated yellow) benefiting from several possible interaction sites in the BIS-linker (illuminated green) proximity, serving as an illustrative explanation for the strong adsorption amplification due to the cross-linker (see Table 1 and Fig. 5). Nitro-oxygens of NP− can form hydrogen bonds (dashed orange lines depict potential hydrogen bond formation in this configuration) with numerous amide hydrogens, whereas the non-polar aromatic ring is surrounded by hydrophobic environment, i.e., isopropyl groups, (highlighted by bubbles) of the flexible PNIPAM side-chains. An aromatic ring–backbone contact has been observed but less frequently than the presented scenario. NP− can stay in such a conformation (with interchanging binding sites) for several tens of nanoseconds. |
The least polar compound among them, nitrobenzene, shows the most substantial amplification of binding to the cross-linker at higher concentrations. NB is known to form NB–NB pairs and stacks of the aromatic rings,69 resulting thus in positive cooperativity for local adsorption (refer to earlier work38 for further explanation). Note that the bulk concentration of ρ0 = (28 ± 2) mM might have exceeded the solubility of nitrobenzene in water. At 298 K the experimental value is 16 mM, but computer simulations can overestimate the solubility (115 mM).70
NP0 also performs stacking (Fig. 4c), but due to its additional OH-tail, it has a higher water solubility and is thus less probable to aggregate. In stark contrast, the NP− adsorption to the whole network unit drastically drops at higher concentrations due to their electrostatic repulsion. This is an example of strong negative cooperativity of adsorption at higher concentrations. Note that a real hydrogel may change in size (in particular close to its VPTT) because of the solute–polymer interactions and that solutes may occupy a non-negligible volume, which in return limit the solute adsorption.20,35,71,72
![]() | (10) |
The number of particles Nin inside the gel can be assessed using the total solute adsorption as
Nin = Γtot + ρ0Vgel. | (11) |
Γtot = NmerΓmer + NxlinkΓxlink, | (12) |
![]() | (13) |
Considering now a defect-free diamond lattice network architecture22,49 of the hydrogel, we can deduce the functional form of the monomer concentration vs. the cross-linker ratio, i.e., ρmer → ρmer(α), see Appendix B. For different adsorption coefficient pairs () and in dependence on the cross-linker ratio, K is visualized in Fig. 7. We find that K and α can have a non-linear relation and even a non-monotonic behavior. The reason is that higher cross-linker ratios directly enhance the influence of
, and additionally, as already discussed, increase the PNIPAM concentration ρmer(α), promoting the influence of
. If now
and
have even different signs, i.e., a solute, for example, is preferentially desorbed from the polymer but adsorbed by cross-linker then naturally non-monotonic behavior must occur.
![]() | ||
Fig. 8 Chemical structures of PNIPAM and BIS. The superscript indices differentiate atoms regarding their partial charges, shown in Table 2. |
Typical values for cross-linker ratios in experiments range from roughly 0.02 to 0.2. In our model (see Appendix B), this corresponds to volume fractions ranging from approximately 0.03 to 0.75 with an almost linear relation to α in this interval. Thus the plotted region in Fig. 7 is quite reasonable for demonstrating the non-linear and non-monotonous α-dependencies of the partition ratio. In particular, with positive adsorption coefficients, like all nitro-aromatics have, we find that the partition ratio monotonically increases with larger cross-linker ratios, exemplified by nitrobenzene in Fig. 7.
Selective solute–cross-linker binding affinities are not solely responsible for an increasing partition ratio when increasing the cross-link ratio. As an illustration, we show scenarios of hypothetical solutes that have either zero adsorption to cross-linkers or zero adsorption to the chains. For small values of α, the coefficient has greater impact on partitioning increase than
. In the case of benzene (similarly hexane and butane), where we find a positive chain adsorption, but repulsion from the cross-linker, the partitioning reaches a plateau at α = 0.2. Weaker chain adsorption, or stronger cross-linker repulsion can lead to a maximum in the plotted range, which is exemplified by the hypothetical solute with
and
. The very opposite case, i.e., cross-linker affinity in combination with chain avoidance, as we find for the tested ion pair Na+/Cl−, exhibits a minimum.
Summing up, the adsorption coefficients and
determine the gradient and concavity of the solute partitioning in dependence on the cross-linker ratio, assuming homogeneous and diamond lattice-like network structure. We conclude that partitioning vs. the cross-linker ratio may be complex and non-monotonous, exhibiting minima and maxima and intercepting the K = 1 line.
Our investigation focuses on very low solute concentrations, though the response of the polymer to the penetrants might not be negligible. From experiments71,72,75 it is known, that solutes may change the hydrogel's VPTT, which has additionally been demonstrated in computer simulations.20,35
Nevertheless, our idealized approach tackling the partitioning does allow for an indirect comparison to experimental data. One experiment on the rate of the nitrobenzene reduction in an (N-isopropylacrylamide-co-acrylic-acid (PNIPAM-co-AAc)) nanoreactor76 shows an increase in the reduction rate with increasing cross-link (BIS) density, which is attributed to the higher nitrobenzene concentration inside the hydrogel. Parasuraman et al.77 used a very similar hydrogel (PNIPAM-co-AAc-BIS) and proved the increased dye uptake (Orange II) with increasing cross-link ratio. Both studies qualitatively support our findings. They, however, have in common that the initial increase of the reduction rate and the dye uptake, respectively, apparently saturates for higher cross-link degrees. This effect is not captured by our model and might result from steric hindrances, i.e., undersized pore/mesh size of the polymer architecture and already occupied adsorption sites for higher solute concentrations.
After qualitatively confirming the impact of the cross-link ratio on the partitioning of the aromatic compounds, we will now assess the comparison in terms of absolute values. Experimentally, partition ratios have been reported for several molecules containing aromatic rings. A study by Molina et al.52 retrieved K in PNIPAM–BIS-hydrogels (α = 2%) for probe drugs (tryptophan, propranolol chloride, dansyl chloride, methyl orange, riboflavin, and ruthenium-tris(2,2′-bipyridyl)dichloride), which contain two to six aromatic rings as well as polar and/or charged residues. The partition ratio, depending on the compound, ranges from roughly 4.6 to 10.
Comparing to our perfect network model, the much smaller NB and NP− show partition ratios of approximately 1.3 and 1.8, respectively, at α = 2%, and 2.7 and 5.7 at α = 5% in the low dilution limit (Nsolute = 1). For Nsolute = 20, K is about 3.7 at α = 2% for NB. It is expected that larger molecules at higher concentrations, as established in the mentioned experiments, will lead to higher partition ratios78 and can thus be regarded as supportive of our results. Furthermore, the adsorption increase due to positive cooperativity (e.g., NB) has been shown for methylene blue in a superabsorbent hydrogel.79
The salt partition ratios in 1% cross-linked PNIPAM–BIS gels at room temperature have been reported80 and amount to KLiCl = 0.97 ± 0.05, KKCl = 0.91 ± 0.05 and KNaCl ≈ 0.95, i.e., just below unity as in our prediction for sodium chloride.
However, the non-monotonicity of the partition ratio in dependence on the cross-link ratio predicted by our model has not been reported by experimentalists so far and is yet to be tested.
Comparing the cross-linker and monomer effects on adsorption, we find different scenarios. Apolar species show small attraction to chain monomers and slight repulsion from the cross-linker region. Sodium chloride behaves the opposite, it has negative chain adsorption but is attracted towards the cross-linker. The strongest adsorbing solutes, the nitro-aromatics, adsorb to all parts of the polymer and show the highest binding affinity, which is promoted by hydrophobic interactions between the aromatic ring and PNIPAM's isopropyl groups as well as by hydrogen bonds between the nitro-oxygens and the amide groups. The adsorption at the cross-linker relative to a single PNIPAM monomer adsorption, spans from Γxlink/Γmer ≈ 2 (NB) to Γxlink/Γmer ≈ 10 (NP0, NP−). This indicates that the cross-linker can significantly enhance the overall adsorption to the network unit. Hence, for solutes that have a significant affinity to PNIPAM chains already, the dense cross-linker region, where many-body attractions are at play, amplifies the local adsorption by even an order of magnitude. Thereby we confirm the ‘vertex trapping’ effect that has been first reported in generic coarse-grained simulations of polymer networks.24–28
In the case of the nitro-aromatics, we furthermore performed simulations with higher solute concentrations to estimate cooperative adsorption effects. Nitrobenzene shows enhanced aromatic stacking at the cross-linker and the adsorption is elevated in a superlinear fashion with increasing concentration. Nitrophenol shows similar, positive cooperativity but a less pronounced behavior. For both NB and NP0 the cross-linker promotes higher positive cooperation effects than single chains. In contrast, in the case of the negatively charged nitrophenolate, we observe less adsorption at higher concentrations due to negative cooperativity stemming from the electrostatic repulsion.
The adsorption coefficients for cross-linker and chain monomers in the low concentration regime were used to estimate partition ratios of the solutes within an idealized, homogeneous diamond-lattice macrogel, which allowed a comparison with experimental findings. In our model, we found that highly adsorbing substances like nitro-aromatics have a partition ratio ranging from 2 to 5 at a cross-linker concentration of 5%. Solutes with adsorption coefficients of opposite signs may show non-monotonic behavior as a function of the cross-linker ratio: positive/negative chain adsorption and negative/positive cross-linker adsorption leads to a maximum/minimum in the partition ratio. These yet poorly known features should be considered in future experiments and modeling of hydrogels as they play an important role for the fine-tuning of solute uptake within the needs of the desired function and application.
OPLS-AA46 | HF-6-31G(d) | OPLS-QM231 | Charges used in this work | ||
---|---|---|---|---|---|
BIS | PNIPAM | PNIPAM | |||
C1 | −0.12 | −0.22 | −0.20 | −0.18 | −0.18 |
H1 | 0.06 | 0.07 | 0.08 | 0.09 | 0.09 |
C2 | −0.06 | −0.13 | −0.07 | 0.00 | 0.00 |
H2 | 0.06 | 0.06 | 0.05 | 0.05 | 0.05 |
C3 | 0.50 | 0.81 | 0.80 | 0.50 | 0.50 |
O | −0.50 | −0.61 | −0.65 | −0.57 | −0.57 |
N | −0.50 | −0.69 | −0.84 | −0.57 | −0.57 |
HN | 0.30 | 0.39 | 0.39 | 0.33 | 0.33 |
C4 | 0.14 | — | 0.64 | 0.36 | 0.36 |
H4 | 0.06 | — | −0.01 | 0.06 | 0.06 |
C5 | −0.18 | — | −0.52 | −0.32 | −0.32 |
H5 | 0.06 | — | 0.12 | 0.08 | 0.08 |
C6 | — | 0.06 | — | — | 0.40 |
H6 | 0.06 | 0.14 | — | — | 0.06 |
Recapturing the results for the adsorptions around single chains reported by our group before,38 the reader may compare the standard OPLS-AA force field for PNIPAM polymers with the further optimized OPLS-QM2 version31 employed in this work. The qualitative trends, i.e., size and polarity dependence as well as the strong nitro aromatic binding affinity remain. However, comparing absolute numbers for aromatic compounds, the standard force field38 shows a roughly twice as high adsorption coefficient to the chain monomers. We attribute this effect to more polar amide groups in the OPLS-QM2 force field and hence to more hydrophilic behavior. Moreover, the adsorption of NP− to PNIPAM (in the OPLS-QM2 version) is significantly larger owing to its polar nitro group.
![]() ![]() | (14) |
![]() | (15) |
By knowing nmer(α), we can further approximate the polymer volume fraction, which allows us to identify physically meaningful values of α and K. Using the water profile (Fig. 3) we extract the excluded volume per monomer as Vex,mer = 0.167 nm3 and assume the BIS’ volume to scale with the number of heavy atoms (without hydrogens) compared to a PNIPAM monomer (11 vs. 8), yielding Vex,xlink = 0.230 nm3. The excluded volume in one unit cell is then vex = 8Vex,xlink + nmer(α)Vex,mer and the polymer volume fraction for different values of α is obtained as ϕp = vex/vgel (Fig. 7).
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