Skip to main content
Polymers logoLink to Polymers
. 2023 Nov 28;15(23):4560. doi: 10.3390/polym15234560

Bead–Spring Simulation of Ionomer Melts—Studying the Effects of Chain-Length and Associating Group Fraction on Equilibrium Structure and Extensional Flow Behavior

Supun S Mohottalalage 1, Andrew P Saab 1, Amitesh Maiti 1,*
Editor: Juan J Freire1
PMCID: PMC10708384  PMID: 38232005

Abstract

Ionomers are associative polymers with diverse applications ranging from selective membranes and high-performance adhesives to abrasion- and chemical-resistant coatings, insulation layers, vacuum packaging, and foamed sheets. Within equilibrium melt, the ionic or associating groups are known to form thermally reversible, associative clusters whose presence can significantly affect the system’s mechanical, viscoelastic, and transport properties. It is, thus, of great interest to understand how to control such clusters’ size distribution, shape, and stability through the designed choice of polymer architecture and the ionic groups’ fraction, arrangement, and interaction strength. In this work, we represent linear associating polymers using a Kremer–Grest type bead–spring model and perform large-scale MD simulations to explore the effect of polymer chain-length (l) and fraction (fs) of randomly placed associating groups on the size distribution and stability of formed clusters. We consider different chain-lengths (below and above entanglement), varying fractions of associating groups (represented by ‘sticky’ beads) between 5 and 20%, and a fixed sticky–sticky nonbond interaction strength of four times that between regular non-associating beads. For all melts containing associating groups the equilibrium structure factor S(q) displays a signature ionomer peak at low wave vector q whose intensity increases with increasing fs and l. The average cluster size Nc increases with fs. However, the effect of chain-length on Nc appears to be pronounced only at higher values of fs. Under extensional flows, the computed stress (and viscosity) is higher at higher fs and l regardless of strain rate. Beyond a critical strain rate, we observe fragmentation of the associative clusters, which has interesting effects on the stress/viscous response.

Keywords: associative polymers, bead–spring model, molecular dynamics, extensional rheology

1. Introduction

Associating polymers are smart, responsive materials that incorporate reversibly associative functional groups. They have been used in diverse technologies ranging from water purification [1,2] to desalination [3,4], fuel cells [5,6], biomedical sensors [7,8], flow batteries [9,10], enhanced oil recovery in petroleum industry [11,12], and self-healing [13,14] applications. Ionomers are an important subclass of associating polymers in which less than 20% of the backbone atoms are bonded to pendant groups that are ionic, with nonbonded counterions maintaining charge neutrality. The associating groups in ionomers tend to form aggregates (also referred to as clusters) [15] within the bulk microstructure, as have been captured by previous theoretical [16,17,18], experimental [19,20,21,22,23,24], and simulation [25,26,27,28,29] studies. One of the first theoretical models of cluster formation in ionomer melts was proposed decades ago by Eisenberg [16,17]. In this model, the associating groups first form multiplets, which grow into clusters. The sizes, shapes, and stability of the clusters are governed by factors such as backbone flexibility and the fraction and binding strength of the associating groups [16]. Experimental studies by Winey et al. [19] later detected spherical aggregates in small-angle X-ray scattering (SAXS) and scanning transmission electron microscope (STEM) images. Recent simulation studies [26,27,28,29] have also captured the formation of clusters, and the corresponding computed static structure factor S(q) was in good agreement with available experimental results.

Besides being structurally interesting, the formation of clusters can lead to significant changes to the physical, mechanical, and viscoelastic properties of an ionomer melt. Over the past two decades, several studies [21,22,23,26,29,30,31,32,33] have captured the effects of associating groups on the polymer structure, dynamics, and rheology. For sulfonated polystyrene (SPS) systems, SAXS measurements revealed a peak under light sulfonation levels [21], indicative of the formation of clusters. As the sulfonation fraction was increased, the feature developed into a sharp, intense peak. More recently, there have been a number of computational explorations of cluster formation in associating polymer melts using both coarse-grained [31] and fully atomistic [25,26,29] simulations. In particular, Senanayake et al. [31] investigated the structure and dynamics of melts of fully flexible, linear associating polymers using the Kremer–Grest bead–spring model in which the interaction strength between associating beads was varied from 1 to 20 kBT. It was found that with an increase in association strength the average cluster size increases, which is accompanied by a dramatic decrease in the mobility of the polymer chains. Fully atomistic molecular dynamics have also been used to explore associating polymer melts. For instance, Agrawal et al. [25] and Mohottalalage et al. [26] investigated the structure factor S(q) of SPS melts below the entanglement length and found excellent agreement with available experimental data. Mohottalalage et al. [26] further demonstrated that parameters such as the size of the clusters and the number of unique polymer chains associated with clusters can have a considerable impact on the local dynamics of the polymer.

Understanding the rheological properties of associating polymers is also of great interest, given that these materials are hard to formulate and process. Weiss and coworkers performed a few of the first rheological experiments in this field [22,32,33,34,35]. They observed that a small number of ionic groups can significantly impact the viscoelastic behavior of SPS. Ling et al. [35] studied the extensional behavior of SPS melts (~6.5 mol % sulfonation) and observed pronounced extensional stress effects for ionomers at higher strain rates and lower temperatures. Further investigations revealed that the strain at the stress maximum for ionomers is substantially lower than that in non-sulfonated polystyrene (PS) melts. They speculated that the stress maximum could be due to disruptions of the ionomer-cluster network [35]. Yu et al. [33] studied the linear viscoelastic behavior of lightly (~0.11–1.71 mol %) sulfonated SPS ionomers. They reported that the rubbery modulus increased with an increasing sulfonation percentage and followed the classical rubber elasticity theory. A recent rheology study by Mohottalalage et al. [30] for coarse-grained melts of fully flexible associating polymers showed that while the equilibrium cluster size expectedly increases with an increase in association strength, extensional flow leads to a dynamic equilibrium in which the clusters break and reform continuously. This study was recently extended to SPS systems using all-atomistic simulations [36].

The present work aims at exploring a few aspects of ionomer systems that have not been systematically studied before, i.e., the effect of the chain-length (below and above entanglement length) and the fraction of associating groups on the equilibrium-structure and the viscoelastic properties of associating polymer melts under extensional flow. Given significant computational requirements, we have employed bead–spring-level simulations here, with the possibility of all-atom modeling of technologically important ionomer materials in our future efforts.

2. Methodology

We performed equilibrium and non-equilibrium MD simulations using the Large-scale Atomic/Molecular Massively Parallel Simulator (LAMMPS) [37] and the standard Kremer–Grest bead–spring model [38,39], which describes the fully flexible linear polymer chains. In this model, each polymer chain is represented by a string of beads, each bead physically representing a Kuhn monomer. Nearby beads (with 1–2, 1–3, and 1–4 exclusion for neighboring intra-chain beads) interact via a pairwise nonbond Lennard-Jones (LJ) potential within a cutoff range of 2.5σ, while neighboring beads on a chain are connected by finitely extensible nonlinear elastic (FENE) springs with a mean bond length of b ≈ 0.96σ. Two types of beads are employed, i.e., ‘regular beads’ representing non-associating groups α and ‘sticky beads’ representing associating groups β. While the FENE spring potential and the mass are the same for all beads, the LJ potential interaction is stronger for the sticky beads. In this work, we made the choice εββ=4εαα with the cross-term εαβ=εαα. Such interactions are typical of ionomer association strengths that are known to yield cluster formation [30,31]. In the discussion below, we express each quantity in reduced units, i.e., mass is expressed in units of mass per bead m, length is expressed in units of LJ parameter σ, energy is expressed in units of LJ parameter εαα, temperature is expressed in units of kBT/εαα, and time is expressed in units of τ=σm/εαα.

We studied melts equilibrated at temperature T = 1 and density ρ ≈ 0.87, using a time step Δt = 0.001. Each melt was represented by 500 chains of equal length. Four different chain-lengths were explored, i.e., l = 20, 40, 80, and 120 beads. To understand the effect of association group fraction on the size and stability of formed clusters, we considered three different sticky fractions, i.e., fs = 5, 10, and 20%, with sticky beads placed randomly along the chains.

For each system, the initial structures were created using the ‘standard’ procedure described in section V of Auhl et al. [40]. Briefly, the procedure consists of four steps: (1) Start from an ensemble of chains with the correct end-to-end distance, i.e., R2(N)(N1). (2) Place the chains randomly in a large simulation box (i.e., at much lower density than the equilibrium bulk density). (3) Introduce a soft excluded-volume potential between non-connected beads, which is of the functional form A1+cosπr/rc (for rrc=21/6σ) with an initial amplitude A=4εαα, which is linearly increased to a final value of A100εαα (‘push-off’) over a short time interval (1020 τ). This procedure leads to an elimination of all initial atom-overlaps and results in large enough inter-monomer distances that enables using the LJ potential without any instabilities. (4) Relax the system with the full LJ potential with a short MD run. The ‘standard’ procedure described above is sufficient for chains of length up to 120 as studied in the present work. For much longer chains (500 or above), a more sophisticated procedure could become necessary [40]. Each initial structure was subjected to an equilibration run of length 0.4×106τ (i.e., 0.4×109 time steps). To ensure that a state of equilibrium had been reached, we monitored the time-evolution of a few structural characteristics, including the average chain end-to-end distance, radius of gyration, and radial distribution function. Following equilibration, a production NVT run of length 106τ was carried out for each system.

Finally, extensional flow simulations on the melt systems were performed by employing the Generalized Kraynik–Reinelt (GKR) [41,42] boundary conditions under a constant Hencky strain rate ε˙lnΛ/t, where Λ is the stretch ratio along the z direction. The GKR boundary condition enables the achievement of much larger strains without collapsing the simulation box in the contracting directions [30,41,42,43]. The equations of motion under flow were integrated using the g-SLLOD algorithm [44,45] as implemented in LAMMPS. We computed quantities such as extensional stress σE=σzzσxx+σyy/2 and the transient extensional viscosity ηex(ε)=σE/ε˙. To correlate with experimental results [46,47], we expressed the applied strain rate in terms of a dimensionless Weissenberg number [48,49,50] defined as Wi=ε˙τR, where τR is the Rouse time, given by τR=τeZ2, where Z=l/le is the average number of entanglements per chain and τe the entanglement time. For linear and fully flexible bead–spring polymers, le~84 [51,52] and τe~104τ [53], which enables relating Wi to applied strain rates ε˙. In this work we vary Wi from 4 to 32. From the above value of le we also note that our chosen chain-lengths of l=20, 40, 80, 120 cover cases of both below and above entanglement length.

3. Results and Discussion

3.1. Equilibrium Study

Figure 1 illustrates snapshots of clusters formed in melts of chains with varying lengths and sticky fractions. We define a cluster as a collection of sticky beads such that each sticky bead has at least one sticky bead neighbor within a distance of 1.5σ. The clusters in Figure 1 are colored based on their size (i.e., the number of sticky beads present within the cluster) using a red–green–blue color scheme, with single sticky beads in red and medium-sized and larger clusters in green and blue, respectively. Even at fs= 5% significant clustering effects are observed (Figure 1 (left)). Such results are similar to Kirkmeyer et al. [19] who observed ionic aggregates in ionomers using STEM imaging. Figure 1 also shows that the average cluster size increases with increase in fs, while the effect of chain-length on overall cluster sizes appears weak. The formation of a typical cluster about average size in a polymer melt corresponding to l=120 and fs= 5%. is shown in Supplementary Section (Video S2).

Figure 1.

Figure 1

Snapshots of associated (sticky) clusters in melts for chain-lengths: l=20, 40, and 120 for sticky fractions; fs=5% (left), 10% (middle), and 20% (right). Red, green, blue indicates isolated, medium-sized, and large clusters.

To more precisely quantify the effect of chain-length l and sticky fraction fs on cluster sizes, we have computed the cluster size distribution within each melt. Figure 2a plots the average cluster size Nc as a function of the sticky fraction fs, while Figure 2b plots the size distribution of clusters nNc (normalized by the total number of beads in the simulation cell) for fs=5% and 20%.

Figure 2.

Figure 2

(a) Average cluster size Nc vs. sticky fraction fs (%), for different chain-lengths l. (b,c) size distribution of clusters nNc (normalized by the total number of beads) as a function of cluster size Nc for two different sticky fractions fs.

It is interesting to note that, at a low sticky fraction (fs=5%), the average cluster size (and the cluster size distribution on whole) is insensitive to the polymer chain-length l. However, at higher sticky fractions, the average cluster-size decreases monotonically with chain-length, with a sharper decrease around and above the entanglement length. Figure 2c provides deeper insight into this phenomenon by showing that the number of ‘isolated sticky beads’ (Nc=1) is significantly higher for l=120 as compared to l=40. One can attribute such behavior to entanglement-induced constraints to structural relaxation of larger chains as compared to shorter chains, which hinders the aggregation process of sticky beads into larger clusters. Additionally, when comparing Figure 2b,c, one observes a much wider distribution of cluster sizes at a larger sticky fraction (for chains of all sizes), a clear indication of a combinatorically much larger number of choices of cluster formation in the presence of a larger number of associating groups.

To better understand the compactness of the clusters, we computed the sticky bead–sticky bead radial distribution function g(r) (normalized by the total number of sticky beads in the system) as plotted in Figure 3. The first peak, at approximately 1.1σ, corresponds to the shortest distance between two associating beads within a cluster. The intensity of the first peak (Ip1[gr]) is significantly higher than the second and third peaks, which are at approximately 1.9σ and 2.8σ, respectively. The second and the third peaks are broader than the first and correspond to the next neighboring sticky beads within the cluster. From Figure 3, we observe that for smaller fs the intensity of the first peak is higher, which indicates a more compact (i.e., spherical-like) clusters for smaller sticky fractions. At higher fs the clusters are bigger (see Figure 1 and Figure 2) but less compact, i.e., more ‘irregular’ and/or ‘extended’ shapes. With increasing chain-length l, the cluster compactness modestly decreases at small sticky fractions, likely reflecting higher relaxation freedom for smaller chains. However, at high fs (20%) the degree of cluster compactness deteriorates markedly for all chain-lengths, and the chain-length dependence of Ip1[gr] becomes insignificant. A significant departure of cluster shapes from simple spherical has previously been observed in all-atomistic simulations [26,54].

Figure 3.

Figure 3

Sticky bead–sticky bead radial distribution function g(r), for (a) a fixed chain-length (l=20) and different sticky fractions (fs) and (b) for a fixed fs (5%) and different l. (c) Intensity of the first peak Ip1[gr] as a function of fs for different chain-lengths.

To quantify the degree of spatial inter-cluster ordering of the associated clusters within the bulk polymer matrix, we computed the static structure factor of the sticky beads, defined as Sq=N1j=1Nexpiq.rj2, where rj is the position vector of the jth sticky bead, N is the total number of sticky beads in the system, and indicates equilibrium averaging over MD trajectory frames. Results are summarized in Figure 4 for different chain-lengths and sticky fractions. We focus on the small-q region of four wave vectors (in units of 2π/σ) or fewer, which contains a single prominent peak characteristic of inter-cluster correlation. Such an ionomer peak directly correlates with the average Inter-cluster distance and has been previously observed in MD simulations [26,29,54,55] and small-angle X-ray scattering (SAXS) [19,56,57]. Figure 4 displays several interesting results, including the following: (1) For a fixed chain-length, the peak intensity significantly increases with an increase in sticky fraction fs, with little change in peak position. This is likely due to larger cluster sizes at higher sticky fractions while inter-cluster distances remain relatively unchanged. (2) At low sticky fraction (fs=5%), the peak position shifts slightly leftward with an increase in chain-length, while the peak intensity increases. This indicates that, for longer chains, the clusters are distributed with a somewhat higher degree of spatial uniformity and spaced out slightly further apart. And (3) at higher sticky fraction (fs=20%) the dependence of S(q) on chain-length becomes much smaller, likely due to complex effects resulting from a much wider dispersion in cluster sizes.

Figure 4.

Figure 4

Structure factor Sq of sticky beads as a function of momentum transfer wave vector q for different chain-lengths l = 20 (a) and 120 (b) and sticky fractions fs = 5% (c) and 20% (d). We focus on the small-q region (<4 in units of 2π/σ), which displays a single peak representative of inter-cluster ordering.

While the formation of associative clusters is a well-established phenomenon for ionomers, there has been some controversy in the literature about how such clusters affect the equilibrium structural properties of the polymer melt. For instance, certain theories [18,58] predict significant chain expansion in ionomers, while a different theoretical study [59] and a neutron scattering study [60] conclude no apparent chain expansion due to clustering. To shed light on this issue, we computed the equilibrium distribution of the intra-chain end-to-end distance PR. Figure 5 displays results for the unassociated system (fs=0%) and the system with fs=20%. We conclude that the formation of associated clusters has little effect on the overall structural properties of the chains in the melt. In particular, the distribution of end-to-end distance P(R) (Figure 5a) and the rms end-to-end distance R21/2 as a function of chain-length (Figure 5b) follow the behavior expected of Gaussian chains. To analyze the state of chain entanglement within the melts, we have also carried out primitive path (PP) analysis using the Z1+ code from Kröger et al. [61]. Figure 5c plots the average number of entanglements (Z) per chain (defined in terms of topological ‘kinks’) and the average contour length of the primitive path (Lpp) (Figure 5c inset) as a function of chain-length. We observe the expected linear behavior as a function of chain-length with no noticeable effect due to associative clusters. The average number of kinks per chain also appears consistent with an entanglement length le~84, as has been known from previous analysis of such bead–spring melts [51,52].

Figure 5.

Figure 5

Comparing equilibrium structural properties of unassociated (fs=0%;closesolid symbols) and associated (fs=20%;opendash symbols) melts: (a) Distribution function PR of the intra-chain end-to-end distance R; (b) rms end-to-end distance R21/2 as a function of chain-length (l) for different fs; (c) mean number of kinks per chain Z, with the corresponding mean contour length of the primitive paths Lpp shown as inset.

3.2. Ionomers under Extensional Flow

The processing of ionomer melts under different flow conditions is of great technological interest. Several studies in the associating polymer literature have shown significant correlation between the strength of association and rheological properties, including the ease or difficulty of processability [62,63,64,65,66]. To this end, we simulated flow under a constant Hencky strain rate ε˙ (or equivalently, constant Weissenberg number (Wi), see Section 2) for melts of different chain-lengths and sticky fractions. Figure 6 plots the terminal extensional viscosity (ηex=σex/ε˙ for large ε, where σex is extensional stress as defined in Section 2) as a function of Wi. In all cases, we observe shear thinning behavior and an enhancement of viscosity with increasing chain-length and sticky fraction. To provide further insight, we have analyzed the extensional stress response and average cluster size in Figure 7 and Figure 8.

Figure 6.

Figure 6

Terminal extensional viscosity ηex as a function of Weissenberg number Wi for different chain-lengths (l) and sticky fractions (fs). For clarity, four different chain-lengths are split into two figures: (a) l=20, 40; (b) l=80, 120.

Figure 7.

Figure 7

Extensional stress (σex), average cluster size (Nc), and rms intra-chain end-to-end distance (R21/2) as a function of Hencky strain (ε) for melts with a fixed sticky fraction fs=5%: (a) σex for l=40 and different Wi; (b) σex for Wi=8 and different l; (c) Nc and R21/2 for l=40 and different Wi; (d) Nc and R21/2 for Wi=8 and different l.

Figure 8.

Figure 8

Extensional stress (σex) and average cluster size (Nc) as a function of Hencky strain (ε) for different sticky fractions at a fixed strain-rate (Wi=8) for two different chain-lengths (l): (a) σex for l=40; (b) σex for l=120; (c) Nc for l=40; (d) Nc for l=120.

Figure 7a,b show the stress–strain behavior of the fs=5% ionomers for various strain rates (Wi) and chain-lengths (l), respectively. We see a linearly increasing extensional stress σex for (Hencky) strain up to ε~4. With further increase in strain, the stress σex fluctuates around a steady-state value. This steady-state value is used to compute the terminal viscosity ηex in Figure 6. From Figure 7a,b, we see that the steady-state σex increases with increasing strain-rate as well as increasing chain-length. Figure 7c,d display the corresponding mean cluster size Nc and rms end-to-end distance R21/2, which reveal the following: (1) the steady-state average cluster-size decreases both with increasing strain (i.e., flow) rate and with increasing chain-length (MD movie showing the extension of the polymer chain is presented in the Supplementary Section; Video S2), which leads to a larger number of clusters and consequently supports higher levels of extensional stress, and (2) at a given flow rate (Wi=8) longer chains stretch proportionally longer, as evident from the ratio R21/2:l. This phenomenon is likely due to a larger number of clusters in the steady state, which, on an average, leads to a larger tensile pull on the chains along the flow direction.

Figure 8 explores extensional stress and average cluster size at a fixed flow rate (Wi=8) for various sticky fractions fs and two different chain-lengths. We observe that both extensional stress and average cluster-size in steady-state flow increase with increasing sticky fraction fs. Additionally, we also see that at higher sticky fractions (10% and higher) a stress overshoot develops that is not observable at low fs. Such behavior in strongly associating polymers has been documented in previous experimental [22,67,68] and simulation studies, both all-atom [36] and coarse-grained [30].

To gain a deeper perspective on the effect of extensional flow on individual chains, we computed the distribution PR of intra-chain end-to-end distance R. Figure 9 displays these results for systems with chain-lengths l=40 and l=120 for sticky fractions fs=0, 5, 10, 20% for the initially unstrained state (ε=0) and two different strain states (ε=3, 10). For the non-associated melt (fs=0%), we see two different behaviors depending on whether chains are unentangled (l=40) or above entanglement length (l=120), i.e., the unentangled chains do not stretch much under flow relative to its equilibrium, while most chains above entanglement length stretch under flow, as shown by the blue peak. On the other hand, for associated melts the formation of clusters acts as effective cross-links and leads to significant chain stretching (near full extension) with the effect being more pronounced at higher sticky fractions. In all cases, the P(R) distribution appears to reach a steady state profile, which is consistent with the behavior seen in Figure 7 and Figure 8 that display a steady state pattern for ε>4.

Figure 9.

Figure 9

(a) Distribution function P(R) of the intra-chain end-to-end distance R for a fixed strain rate (Wi=8) and different sticky fractions (fs) at three different values of Hencky strain (ε) and two different chain-lengths: (a) l=40; (b) l=120. For clarity, curves for fs=5, 10, and 20% are vertically shifted by 0.15, 0.30, and 0.45, respectively.

Figure 10 shows the cluster-size distributions corresponding to each fs>0 figure in Figure 9. For a clearer display, the plots are split into two size ranges, i.e., 1Nc<10 and Nc10. In both ranges, we see a leftward shift of the size distribution nNc with flow, which results from the flow-induced fragmentation of equilibrium clusters. It is interesting that the largest clusters in the unentangled melt (l=40) under equilibrium (ε=0) are larger than the largest clusters in the longer-chain melts, the size of the former being as large as a few hundred for fs=20%. Even after flow-induced fragmentation, a few large clusters can remain in the unentangled melt. This is likely due to the smaller unentangled chains have higher flexibility in aligning themselves in the flow direction. This leads to stress relaxation in the system and less cluster fragmentation as compared to longer-chain melts (l=120). A higher level of steady-state stress in associated longer-chain melts is subsequently maintained by the presence of a larger number of medium-sized fragmented clusters that act as effective cross-links.

Figure 10.

Figure 10

Cluster size distribution profiles for a fixed strain rate (Wi=8), two different chain-lengths (l=40, 80), three different sticky fractions (fs=5, 10, 20%), and three different strain levels (ε=0, 3, 10). For visual clarity, the curves for different sticky fraction fs are vertically shifted, and the cluster size-ranges are split into two intervals: (a,b) 1Nc<10 and (c,d) Nc10.

4. Conclusions

In this study, bead–spring molecular dynamics simulations were employed to investigate the impact of chain-length (below and above entanglement length) and sticky fraction (up to 20%) on the structure and rheological behavior of associating polymer melts. Employing a sticky–sticky interaction strength of four times that between non-associating groups, we observed the formation of stable clusters at a sticky fraction fs of just 5%. With increasing fs the average cluster-size increases, while the cluster size distribution becomes wider. We also found that at low fs the average cluster-size and the size distribution are relatively insensitive to chain length l, while at higher fs smaller l leads to more efficient (and therefore larger) clusters. To characterize the compactness of clusters we computed the sticky–sticky radial distribution function g(r) in equilibrium melts and found that more compact clusters form at lower fs, while at higher fs the clusters are bigger but less compact, i.e., more irregular and/or extended shapes. With increasing chain-length l the cluster compactness modestly decreases at small sticky fractions, likely due to more restricted chain relaxation. However, at high fs (20%) the degree of cluster compactness deteriorates irrespective of chain-length. To quantify the uniformity and separation in the spatial distribution of clusters, we computed the static structure factor S(q) and found that at lower fs (5%) the clusters in longer-chain melts are distributed with a somewhat higher degree of spatial uniformity and spaced out slightly further apart as compared to in unentangled melts. However, at higher fs such dependence on chain-length becomes less distinguishable due to complex effects of a much wider dispersion in cluster-sizes. To characterize whether cluster formation has any effects on the global structural properties of the individual chains, we computed the distribution P(R) of the intra-chain end-to-end distance R and found that clusters have little effect on such distribution. This likely implies that chain relaxations involved in cluster formation are ‘local’ in nature and do not involve large-scale rearrangements relative to unassociated melts.

Finally, under extensional flows all associated systems exhibited shear-thinning with a steady-state behavior for (Hencky) strain levels ε>4. The corresponding viscosity was found to be higher for larger sticky-fraction fs and longer chain-lengths l, as expected. Higher strain-rates were found to result in greater fragmentation of equilibrium clusters, which in dynamical equilibrium led to a decrease in average cluster-size. In unentangled melts (small chain-lengths) a higher level of stress relaxation occurs through increased flexibility of individual chains in aligning parallel to the flow direction. This leads to less cluster fragmentation and, thus, fewer but larger clusters. In contrast, for longer-chain melts under extensional flow a larger number of medium-sized fragmented clusters form, which act as effective cross-links. This, plus an additional effect of topological constraints due to entanglements, supports a higher level of extensional stress in longer-chain melts. Results on equilibrium and flow properties such as these can provide useful insights on how to control and optimize the processing of associated polymer melts for various applications.

Supplementary Materials

The following supporting information can be downloaded at https://www.mdpi.com/article/10.3390/polym15234560/s1, Video S1: Movie illustrating the formation of three average-sized random clusters in a polymer melt of chain-lengths l=120 and associating (i.e., sticky) bead fraction fs=5%. For clarity of visualization, only the sticky beads are displayed. The movie corresponds to a MD simulation run of 0.35×106τ (i.e., 0.35×109 time-steps); Video S2: Movie showing the extension of polymer chains in a melt with l=120 and fs=20%, under extensional strain-rate Wi = 32, for true (Hencky) strain levels up to ε=10. Different colors have been employed to distinguish different polymer chains.

Author Contributions

Conceptualization, S.S.M. and A.M.; Formal analysis, S.S.M.; Writing—original draft, S.S.M.; Writing—review & editing, A.M.; Supervision, A.P.S. and A.M. All authors have read and agreed to the published version of the manuscript.

Conflicts of Interest

The authors declare no conflict of interest.

Funding Statement

This work was performed under the auspices of the U.S. Department of Energy by Lawrence Livermore National Laboratory under Contract DE-AC52-07NA27344.

Footnotes

Disclaimer/Publisher’s Note: The statements, opinions and data contained in all publications are solely those of the individual author(s) and contributor(s) and not of MDPI and/or the editor(s). MDPI and/or the editor(s) disclaim responsibility for any injury to people or property resulting from any ideas, methods, instructions or products referred to in the content.

References

  • 1.Janietz S., Brening T., Schiestel T., Götz T. Block copoly (phenylquinoxaline) s as potential ionomers for proton exchange membranes. Polymer. 2023;271:125794. doi: 10.1016/j.polymer.2023.125794. [DOI] [Google Scholar]
  • 2.Cha J.-E., Jang S., Seo D.-J., Hwang J., Seo M.H., Choi Y.-W., Kim W.B. A reinforced composite membrane of two-layered asymmetric structure with Nafion ionomer and polyethylene substrate for improving proton exchange membrane fuel cell performance. Chem. Eng. J. 2023;454:140091. doi: 10.1016/j.cej.2022.140091. [DOI] [Google Scholar]
  • 3.Khan Z.U., Moronshing M., Shestakova M., Al-Othman A., Sillanpää M., Zhan Z., Song B., Lei Y. Electro-deionization (EDI) technology for enhanced water treatment and desalination: A review. Desalination. 2023;548:116254. doi: 10.1016/j.desal.2022.116254. [DOI] [Google Scholar]
  • 4.Verma A., Parashar A., Van Duin A.C. Graphene-Reinforced Polymeric Membranes for Water Desalination and Gas Separation/Barrier Applications, Innovations in Graphene-Based Polymer Composites. Elsevier; Amsterdam, The Netherlands: 2022. pp. 133–165. [Google Scholar]
  • 5.Braaten J.P., Kariuki N.N., Myers D.J., Blackburn S., Brown G., Park A., Litster S. Integration of a high oxygen permeability ionomer into polymer electrolyte membrane fuel cell cathodes for high efficiency and power density. J. Power Sources. 2022;522:230821. doi: 10.1016/j.jpowsour.2021.230821. [DOI] [Google Scholar]
  • 6.Soleymani A.P., Reid M., Jankovic J. An Epoxy-Free Sample Preparation Approach to Enable Imaging of Ionomer and Carbon in Polymer Electrolyte Membrane Fuel Cells. Adv. Funct. Mater. 2023;33:2209733. doi: 10.1002/adfm.202209733. [DOI] [Google Scholar]
  • 7.Cánovas R., Blondeau P., Andrade F.J. Modulating the mixed potential for developing biosensors: Direct potentiometric determination of glucose in whole, undiluted blood. Biosens. Bioelectron. 2020;163:112302. doi: 10.1016/j.bios.2020.112302. [DOI] [PubMed] [Google Scholar]
  • 8.Komkova M.A., Eliseev A.A., Poyarkov A.A., Daboss E.V., Evdokimov P.V., Eliseev A.A., Karyakin A.A. Simultaneous monitoring of sweat lactate content and sweat secretion rate by wearable remote biosensors. Biosens. Bioelectron. 2022;202:113970. doi: 10.1016/j.bios.2022.113970. [DOI] [PubMed] [Google Scholar]
  • 9.Kim J.Q., So S., Kim H.-T., Choi S.Q. Highly ordered ultrathin perfluorinated sulfonic acid ionomer membranes for vanadium redox flow battery. ACS Energy Lett. 2020;6:184–192. doi: 10.1021/acsenergylett.0c02089. [DOI] [Google Scholar]
  • 10.Yang S.-H., Yang D.-S., Yoon S.J., So S., Hong S.-K., Yu D.M., Hong Y.T. TEMPO radical-embedded perfluorinated sulfonic acid ionomer composites for vanadium redox flow batteries. Energy Fuels. 2020;34:7631–7638. doi: 10.1021/acs.energyfuels.0c00999. [DOI] [Google Scholar]
  • 11.Zhong H., He Y., Yang E., Bi Y., Yang T. Modeling of microflow during viscoelastic polymer flooding in heterogenous reservoirs of Daqing Oilfield. J. Pet. Sci. Eng. 2022;210:110091. doi: 10.1016/j.petrol.2021.110091. [DOI] [Google Scholar]
  • 12.Zhong H., Li Y., Zhang W., Yin H., Lu J., Guo D. Microflow mechanism of oil displacement by viscoelastic hydrophobically associating water-soluble polymers in enhanced oil recovery. Polymers. 2018;10:628. doi: 10.3390/polym10060628. [DOI] [PMC free article] [PubMed] [Google Scholar]
  • 13.Roels E., Terryn S., Iida F., Bosman A.W., Norvez S., Clemens F., Van Assche G., Vanderborght B., Brancart J. Processing of Self-Healing Polymers for Soft Robotics. Adv. Mater. 2022;34:2104798. doi: 10.1002/adma.202104798. [DOI] [PubMed] [Google Scholar]
  • 14.Banshiwal J.K., Tripathi D.N. Self-healing polymer composites for structural application. In: Sahn D., editor. Functional Materials. Volume 10. IntechOpen; London, UK: 2019. pp. 1–13. [Google Scholar]
  • 15.Eisenberg A., Kim J.-S. Introduction to Ionomers. Wiley; New York, NY, USA: 1998. [Google Scholar]
  • 16.Eisenberg A. Clustering of ions in organic polymers. A theoretical approach. Macromolecules. 1970;3:147–154. doi: 10.1021/ma60014a006. [DOI] [Google Scholar]
  • 17.Eisenberg A., Hird B., Moore R. A new multiplet-cluster model for the morphology of random ionomers. Macromolecules. 1990;23:4098–4107. doi: 10.1021/ma00220a012. [DOI] [Google Scholar]
  • 18.Dreyfus B. Model for the clustering of multiplets in ionomers. Macromolecules. 1985;18:284–292. doi: 10.1021/ma00144a029. [DOI] [Google Scholar]
  • 19.Kirkmeyer B.P., Weiss R.A., Winey K.I. Spherical and vesicular ionic aggregates in Zn-neutralized sulfonated polystyrene ionomers. J. Polym. Sci. B Polym. Phys. 2001;39:477–483. doi: 10.1002/1099-0488(20010301)39:5&#x0003c;477::AID-POLB1021&#x0003e;3.0.CO;2-M. [DOI] [Google Scholar]
  • 20.Winey K.I., Laurer J.H., Kirkmeyer B.P. Ionic Aggregates in Partially Zn-Neutralized Poly (ethylene-r an-methacrylic acid) Ionomers: Shape, Size, and Size Distribution. Macromolecules. 2000;33:507–513. doi: 10.1021/ma991374j. [DOI] [Google Scholar]
  • 21.Lu X., Steckle W., Weiss R. Ionic aggregation in a block copolymer ionomer. Macromolecules. 1993;26:5876–5884. doi: 10.1021/ma00074a008. [DOI] [Google Scholar]
  • 22.Huang C., Chen Q., Weiss R. Nonlinear rheology of random sulfonated polystyrene ionomers: The role of the sol–gel transition. Macromolecules. 2016;49:9203–9214. doi: 10.1021/acs.macromol.6b02057. [DOI] [Google Scholar]
  • 23.Fitzgerald J., Weiss R. Synthesis, properties, and structure of sulfonate ionomers. Polym. Rev. 1988;28:99–185. doi: 10.1080/15583728808085376. [DOI] [Google Scholar]
  • 24.Pregi E., Kun D., Wacha A., Pukánszky B. The role of ionic clusters in the determination of the properties of partially neutralized ethylene-acrylic acid ionomers. Eur. Polym. J. 2021;142:110110. doi: 10.1016/j.eurpolymj.2020.110110. [DOI] [Google Scholar]
  • 25.Agrawal A., Perahia D., Grest G.S. Clustering effects in ionic polymers: Molecular dynamics simulations. Phys. Rev. E. 2015;92:022601. doi: 10.1103/PhysRevE.92.022601. [DOI] [PubMed] [Google Scholar]
  • 26.Mohottalalage S.S., Aryal D., Thurston B.A., Grest G.S., Perahia D. Effects of Ionic Group Distribution on the Structure and Dynamics of Amorphous Polymer Melts. Macromolecules. 2022;55:217–223. doi: 10.1021/acs.macromol.1c02141. [DOI] [Google Scholar]
  • 27.Hall L.M., Stevens M.J., Frischknecht A.L. Effect of polymer architecture and ionic aggregation on the scattering peak in model ionomers. Phys. Rev. Lett. 2011;106:127801. doi: 10.1103/PhysRevLett.106.127801. [DOI] [PubMed] [Google Scholar]
  • 28.Frischknecht A.L., Winey K.I. The evolution of acidic and ionic aggregates in ionomers during microsecond simulations. J. Chem. Phys. 2019;150:064901. doi: 10.1063/1.5085069. [DOI] [PubMed] [Google Scholar]
  • 29.Agrawal A., Perahia D., Grest G.S. Cluster morphology-polymer dynamics correlations in sulfonated polystyrene melts: Computational study. Phys. Rev. Lett. 2016;116:158001. doi: 10.1103/PhysRevLett.116.158001. [DOI] [PubMed] [Google Scholar]
  • 30.Mohottalalage S.S., Clemmer J.T., Perahia D., Grest G.S., O’Connor T. Nonlinear Elongation Flows in Associating Polymer Melts: From Homogeneous to Heterogeneous Flow. Phys. Rev. X. 2022;12:021024. doi: 10.1103/PhysRevX.12.021024. [DOI] [Google Scholar]
  • 31.Senanayake M., Perahia D., Grest G.S. Effects of interaction strength of associating groups on linear and star polymer dynamics. J. Chem. Phys. 2021;154:074903. doi: 10.1063/5.0038097. [DOI] [PubMed] [Google Scholar]
  • 32.Qiao X., Weiss R. Nonlinear rheology of lightly sulfonated polystyrene ionomers. Macromolecules. 2013;46:2417–2424. doi: 10.1021/ma3026496. [DOI] [Google Scholar]
  • 33.Weiss R., Yu W.-C. Viscoelastic behavior of very lightly sulfonated polystyrene ionomers. Macromolecules. 2007;40:3640–3643. doi: 10.1021/ma070136i. [DOI] [Google Scholar]
  • 34.Weiss R., Zhao H. Rheological behavior of oligomeric ionomers. J. Rheol. 2009;53:191–213. doi: 10.1122/1.3003570. [DOI] [Google Scholar]
  • 35.GLing H., Wang Y., Weiss R. Linear viscoelastic and uniaxial extensional rheology of alkali metal neutralized sulfonated oligostyrene ionomer melts. Macromolecules. 2012;45:481–490. [Google Scholar]
  • 36.Mohottalalage S.S., Kosgallana C., Meedin S., O’Connor T.C., Grest G.S., Perahia D. Response of Sulfonated Polystyrene Melts to Nonlinear Elongation Flows. Macromolecules. 2023;56:947–953. doi: 10.1021/acs.macromol.2c02326. [DOI] [Google Scholar]
  • 37.Thompson A.P., Aktulga H.M., Berger R., Bolintineanu D.S., Brown W.M., Crozier P.S., In’t Veld P.J., Kohlmeyer A., Moore S.G., Nguyen T.D. LAMMPS-A flexible simulation tool for particle-based materials modeling at the atomic, meso, and continuum scales. Comput. Phys. Commun. 2021;271:108171. doi: 10.1016/j.cpc.2021.108171. [DOI] [Google Scholar]
  • 38.Grest G.S., Kremer K. Molecular dynamics simulation for polymers in the presence of a heat bath. Phys. Rev. A. 1986;33:3628. doi: 10.1103/PhysRevA.33.3628. [DOI] [PubMed] [Google Scholar]
  • 39.Kremer K., Grest G.S. Dynamics of entangled linear polymer melts: A molecular-dynamics simulation. J. Chem. Phys. 1990;92:5057–5086. doi: 10.1063/1.458541. [DOI] [Google Scholar]
  • 40.Auhl R., Everaers R., Grest G.S., Kremer K., Plimpton S.J. Equilibration of long chain polymer melts in computer simulations. J. Chem. Phys. 2003;119:12718–12728. doi: 10.1063/1.1628670. [DOI] [Google Scholar]
  • 41.Dobson M. Periodic boundary conditions for long-time non-equilibrium molecular dynamics simulations of incompressible flows. J. Chem. Phys. 2014;141:184103. doi: 10.1063/1.4901276. [DOI] [PubMed] [Google Scholar]
  • 42.Nicholson D.A., Rutledge G.C. Molecular simulation of flow-enhanced nucleation in n-eicosane melts under steady shear and uniaxial extension. J. Chem. Phys. 2016;145:244903. doi: 10.1063/1.4972894. [DOI] [PubMed] [Google Scholar]
  • 43.O’Connor T.C., Hopkins A., Robbins M.O. Stress relaxation in highly oriented melts of entangled polymers. Macromolecules. 2019;52:8540–8550. doi: 10.1021/acs.macromol.9b01161. [DOI] [Google Scholar]
  • 44.Evans D.J., Morriss G. Nonlinear-response theory for steady planar Couette flow. Phys. Rev. A. 1984;30:1528. doi: 10.1103/PhysRevA.30.1528. [DOI] [Google Scholar]
  • 45.Daivis P.J., Todd B. A simple, direct derivation and proof of the validity of the SLLOD equations of motion for generalized homogeneous flows. J. Chem. Phys. 2006;124:194103. doi: 10.1063/1.2192775. [DOI] [PubMed] [Google Scholar]
  • 46.Subbotin A.V., Malkin A.Y., Kulichikhin V.G. The Elasticity of Polymer Melts and Solutions in Shear and Extension Flows. Polymers. 2023;15:1051. doi: 10.3390/polym15041051. [DOI] [PMC free article] [PubMed] [Google Scholar]
  • 47.Wen Y.-H., Wang C.-C., Cyue G.-S., Kuo R.-H., Hsu C.-H., Chang R.-Y. Extensional rheology of linear and branched polymer melts in fast converging flows. Rheol. Acta. 2023;62:183–204. doi: 10.1007/s00397-023-01387-y. [DOI] [Google Scholar]
  • 48.O’Connor T.C., Alvarez N.J., Robbins M.O. Relating chain conformations to extensional stress in entangled polymer melts. Phys. Rev. Lett. 2018;121:047801. doi: 10.1103/PhysRevLett.121.047801. [DOI] [PubMed] [Google Scholar]
  • 49.O’Connor T.C., Ge T., Rubinstein M., Grest G.S. Topological linking drives anomalous thickening of ring polymers in weak extensional flows. Phys. Rev. Lett. 2020;124:027801. doi: 10.1103/PhysRevLett.124.027801. [DOI] [PMC free article] [PubMed] [Google Scholar]
  • 50.Borger A., Wang W., O’Connor T.C., Ge T., Grest G.S., Jensen G.V., Ahn J., Chang T., Hassager O., Mortensen K. Threading–unthreading transition of linear-ring polymer blends in extensional flow. ACS Macro Lett. 2020;9:1452–1457. doi: 10.1021/acsmacrolett.0c00607. [DOI] [PubMed] [Google Scholar]
  • 51.Sukumaran S.K., Grest G.S., Kremer K., Everaers R. Identifying the primitive path mesh in entangled polymer liquids. J. Polym. Sci. B Polym. Phys. 2005;43:917–933. doi: 10.1002/polb.20384. [DOI] [Google Scholar]
  • 52.Hoy R.S., Foteinopoulou K., Kröger M. Topological analysis of polymeric melts: Chain-length effects and fast-converging estimators for entanglement length. Phys. Rev. E. 2009;80:031803. doi: 10.1103/PhysRevE.80.031803. [DOI] [PubMed] [Google Scholar]
  • 53.Ge T., Robbins M.O., Perahia D., Grest G.S. Healing of polymer interfaces: Interfacial dynamics, entanglements, and strength. Phys. Rev. E. 2014;90:012602. doi: 10.1103/PhysRevE.90.012602. [DOI] [PubMed] [Google Scholar]
  • 54.Bolintineanu D.S., Stevens M.J., Frischknecht A.L. Atomistic simulations predict a surprising variety of morphologies in precise ionomers. ACS Macro Lett. 2013;2:206–210. doi: 10.1021/mz300611n. [DOI] [PubMed] [Google Scholar]
  • 55.Hall L.M., Seitz M.E., Winey K.I., Opper K.L., Wagener K.B., Stevens M.J., Frischknecht A.L. Ionic aggregate structure in ionomer melts: Effect of molecular architecture on aggregates and the ionomer peak. J. Am. Chem. Soc. 2012;134:574–587. doi: 10.1021/ja209142b. [DOI] [PubMed] [Google Scholar]
  • 56.Yarusso D.J., Cooper S.L. Microstructure of ionomers: Interpretation of small-angle x-ray scattering data. Macromolecules. 1983;16:1871–1880. doi: 10.1021/ma00246a013. [DOI] [Google Scholar]
  • 57.Zhou N.C., Chan C.D., Winey K.I. Reconciling STEM and X-ray scattering data to determine the nanoscale ionic aggregate morphology in sulfonated polystyrene ionomers. Macromolecules. 2008;41:6134–6140. doi: 10.1021/ma800805m. [DOI] [Google Scholar]
  • 58.Forsman W.C. Effect of segment-segment association on chain dimensions. Macromolecules. 1982;15:1032–1040. doi: 10.1021/ma00232a016. [DOI] [Google Scholar]
  • 59.Squires E., Painter P., Howe S. Cluster formation and chain extension in ionomers. Macromolecules. 1987;20:1740–1744. doi: 10.1021/ma00174a003. [DOI] [Google Scholar]
  • 60.Visser S.A., Pruckmayr G., Cooper S.L. Small-angle neutron scattering analysis of model polyurethane ionomers. Macromolecules. 1991;24:6769–6775. doi: 10.1021/ma00025a033. [DOI] [Google Scholar]
  • 61.Kröger M., Dietz J.D., Hoy R.S., Luap C. The Z1+ package: Shortest multiple disconnected path for the analysis of entanglements in macromolecular systems. Comput. Phys. Commun. 2023;283:108567. doi: 10.1016/j.cpc.2022.108567. [DOI] [Google Scholar]
  • 62.Hinton Z.R., Alvarez N.J. The Trade-Off between Processability and Performance in Commercial Ionomers. Rheol. Acta. 2019;58:499. doi: 10.1007/s00397-019-01159-7. [DOI] [Google Scholar]
  • 63.Hinton Z.R., Shabbir A., Alvarez N.J. Dynamics of Supramolecular Self-Healing Recovery in Extension. Macromolecules. 2019;52:2231. doi: 10.1021/acs.macromol.8b02423. [DOI] [Google Scholar]
  • 64.Shabbir A., Huang Q., Chen Q., Colby R.H., Alvarez N.J., Hassager O. Brittle Fracture in Associative Polymers: The Case of Ionomer Melts. Soft Matter. 2016;12:7606. doi: 10.1039/C6SM01441K. [DOI] [PubMed] [Google Scholar]
  • 65.Shabbir A., Huang Q., Baeza G.P., Vlassopoulos D., Chen Q., Colby R.H., Alvarez N.J., Hassager O. Nonlinear Shear and Uniaxial Extensional Rheology of Polyether-Ester-Sulfonate Copolymer Ionomer Melts. J. Rheol. 2017;61:1279. doi: 10.1122/1.4998158. [DOI] [Google Scholar]
  • 66.Schaefer C., Laity P.R., Holland C., McLeish T.C. Stretching of Bombyx mori Silk Protein in Flow. Molecules. 2021;26:1663. doi: 10.3390/molecules26061663. [DOI] [PMC free article] [PubMed] [Google Scholar]
  • 67.Wang W., Madsen J., Genina N., Hassager O., Skov A.L., Huang Q. Toward a Design for Flowable and Extensible Ionomers: An Example of Diamine-Neutralized Entangled Poly (styrene-co-4-vinylbenzoic acid) Ionomer Melts. Macromolecules. 2021;54:2306–2315. doi: 10.1021/acs.macromol.0c02408. [DOI] [Google Scholar]
  • 68.Liu S., Cao X., Huang C., Weiss R.A., Zhang Z., Chen Q. Brittle-to-ductile transition of sulfonated polystyrene ionomers. ACS Macro Lett. 2021;10:503–509. doi: 10.1021/acsmacrolett.1c00018. [DOI] [PubMed] [Google Scholar]

Associated Data

This section collects any data citations, data availability statements, or supplementary materials included in this article.

Supplementary Materials


Articles from Polymers are provided here courtesy of Multidisciplinary Digital Publishing Institute (MDPI)

RESOURCES