Abstract
The diffusion of monomerically thin nanorods in polymer melts is studied by molecular dynamics simulations. We focus on the systems where chains are long enough to screen the hydrodynamic interactions such that the diffusion coefficient D∥ for the direction parallel to the rod decreases linearly with increasing rod length l. In unentangled polymers, the diffusion coefficient for the direction normal to the rod exhibits a crossover from D⊥ ~ l−2 to D⊥ ~ l−1 with increasing l, corresponding to a progressive coupling of nanorod motion to the polymers. Accordingly, the rotational diffusion coefficient DR ≈ D⊥l−2 ~ l−4 and then DR ~ l−3 as l increases. In entangled polymers, D⊥ and DR are suppressed for l larger than the entanglement mesh size a. D⊥ ~ l−3 and DR ~ l−5 for l sufficiently above a in agreement with de Gennes’ rod reptation model.
Graphical Abstract
1. Introduction
Incorporation of nanorods into polymers can significantly improve the mechanical,1–3 optical,4–6 and electrical7–11 properties of polymer matrices. While the spatial dispersion and organization of nanorods play critical roles in governing the properties of polymer-nanorod composites,6,12–18 the dynamics of nanorods in polymers is not well understood,19–21 which limits the ability to rationally manipulate the position and orientation of nanorods. Recent experiments also show nanorods could be promising drug delivery carriers due to their superior transport capability in polymeric gels such as mucus,22–26 however, the underlying mechanism is still elusive.
While a continuum theory has been developed for a rod-like colloidal particle in a viscous fluid,27,28 it cannot describe the diffusion of a nanorod in a polymer matrix.20,21,29 A major reason is the nanorod may not be fully coupled to the matrix, resulting in breakdown of the continuum approximation. Such a breakdown has been established for spherical nanoparticles in a polymer matrix.30–37 The friction coefficient for the diffusion of a spherical nanoparticle depends on the ratio of particle diameter to the chain size in unentangled polymer melts and the entanglement mesh size in entangled melts. Likewise, one would expect that the friction coefficient for the diffusion of nanorods in a polymer melt should also depend on the geometric parameters of the rod with respect to the length scales of the polymer. In recent experiments20 and simulations,21 it has already been shown that the diffusion coefficient of nanorods in polymer melts is higher than that predicted by the continuum theory.
One distinctive feature of the diffusion of a nanorod is the emergence of anisotropy in the translational diffusion parallel and normal to the long axis of the rod. In addition to translational diffusion, a nanorod also undergoes rotational diffusion. The rotation couples the parallel and normal components of the translation in the body frame, and the overall translational diffusion is isotropic in the lab frame after the correlation of rod orientation with the initial orientation has decayed.38 Therefore, for nanorods, there are four distinct diffusion coefficients including the overall translational diffusion coefficient DT, the parallel component D∥, the normal component D⊥, and the rotational diffusion coefficient DR. Although the breakdown of the continuum description for nanorods in a polymer matrix has been observed in experiments19,20 and simulations,21 the rich features of the diffusion of nanorods in a polymer matrix have not been well studied.
With the precise control of both nanorod geometry and polymer structure, molecular dynamics (MD) simulations can reveal how nanorod diffusion couples to a polymer matrix. Here we present the results of extensive MD simulations of the diffusion of thin nanorods with a diameter equal to the monomer size in polymer melts in the dilute limit. Rod length l, polymer chain length N, and entanglement length Ne are varied in the simulations. We characterize the scaling of various diffusion coefficients with l and how they are related to each other. We find that the diffusion coefficient of nanorods in polymer melts does not scale with rod length l like that of spherical nanoparticles does with sphere diameter d. This unanticipated behavior reveals the role of particle shape in the coupling of nanoparticles to the polymer matrix.
2. Models and Methods
2.1. Simulation Models
The canonical bead-spring model of polymers39–41 is used in the simulations. Monomers of size σ and mass m interact via the Lennard-Jones (LJ) potential with an interaction strength ϵ, cut-off distance rc = 2.5σ, and characteristic time scale . Chains of N = 2 to 2000 monomers are connected by finitely extensible nonlinear elastic (FENE) bonds. Chain stiffness is varied by a bond bending potential Vθ = kθ(1+cos θ), where θ is the angle between two consecutive bonds. We modeled polymer chains with kθ = 0, 1.5ϵ and 3.0ϵ, which gives a Kuhn length of lK = 1.9σ, 2.9σ and 5.0σ, respectively.42 We also simulated rods in a LJ fluid (N = 1).
Nanorods are modeled as rigid bodies made of beads similar to the monomers. A nanorod of length l is made of l/σ beads of size σ and mass m that are placed along a straight line with regular spacing σ. Nanorod beads interact with polymer beads via a LJ potential with rc = 2.5σ, which promotes the dispersion of nanorods in the melt. Meanwhile, the LJ interaction between beads on two nanorods is purely repulsive (rc = 21/6σ) to prevent the aggregation of nanorods. To equilibrate the nanorods in polymer melts, each sample was simulated with a cubic box of side length L and periodic boundary conditions in all three directions. Two representative samples are visualized in Figures 1a and 1b, respectively. All samples were equilibrated at temperature T = 1.0ϵ/kB and pressure P = 0 except for N = 1 where P = 0.5ϵ/σ3. During the equilibration, a Nosé-Hoover thermostat/barostat was applied to the matrix chains, while a Nosé-Hoover thermostat was used to equilibrate both the translational and rotational degrees of freedom of the rigid nanorods. System parameters for the nanorods in polymer chains with stiffness kθ = 0, 1.5ϵ, and 3.0ϵ are listed in Tables S1, S2, and S3 in Supporting Information (SI), respectively. The number of nanorods was Nr = 27 in all samples except for N = 2000 where Nr = 50, while the number of matrix chains Nc was varied. The volume fraction of the nanorods ϕr = Nrld2/L3, where d and l are the diameter and length of the nanorods, is between 0.004% and 0.07% in all samples. The excluded volume of a nanorod is υexl = l2d, and the volume fraction of the excluded volumes of the nanorods ϕexl = Nrυexl/L3 is less than 2.1% in all samples. The nanorods are well dispersed without any aggregation during our simulations. This is demonstrated by the steady large value of the radius of gyration Rg of the Nr nanorods over time (see Figure S1 of SI). The model used here can be extended to further study the effects of nanorod diameter and interaction strength with polymers in the future.
Diffusion of nanorods in polymer melts at equilibrium was simulated at a fixed volume and a constant temperature T = 1.0ϵ/kB. The temperature of matrix chains was controlled using a Nosé-Hoover thermostat with a damping time 10τ. The temperature for the translation and rotation of a rigid nanorod was maintained by a separate Nosé-Hoover thermostat with a damping time 10τ. Depending on N and l, the simulations were run from 8×104τ to 2×106τ for kθ = 0, from 6×104τ to 1×107τ for kθ = 1.5ϵ, and from 6×104τ to 5×106τ for kθ = 3.0ϵ. The time step was 0.01τ. All the simulations were performed using the LAMMPS simulation package.43
2.2. Calculation of DT, D∥, and D⊥
We computed the mean square displacement (MSD) 〈Δr2(t)〉 = 〈[rcom(t) − rcom(0)]2〉 of the center-of-mass of nanorods as a function of time t in the polymer melts. The overall translational diffusion coefficient DT was extracted from the long-time limit of 〈Δr2(t)〉/6t. 〈Δr2(t)〉 and 〈Δr2(t)〉/6t for two sets of simulations are shown in Figures S2 and S3.
The translational diffusion can be decomposed to parallel and normal components, as schematically shown in Figure 1c. We decomposed the displacement of a nanorod to its parallel and normal components using a numerical procedure similar to that in Ref.38 The procedure is illustrated in Figures 2c and 2d. The parallel component is the displacement of the center-of-mass of nanorods along the rod axis in the body frame, whereas the normal component is the displacement perpendicular to the axis. From t to t + Δt with a time interval Δt, the unit vector along the nanorod changes from u(t) to u(t + Δt), as shown in Figure 2c. The center-of-mass displacement of the nanorod is s(Δt), and the parallel component , where is the average of u(t) and u(t + Δt), as shown in Figure 2d. The displacement s∥(t) along the nanorod axis over time t is obtained by summing the parallel displacements in successive time intervals, i.e., . The parallel component of MSD . The diffusion coefficient D∥ along the rod axis is determined as the long-time limit of .
To obtain the normal component of nanorod displacement, we first rotate the unit vector about an axis uaxis(t) so that aligns with the z-axis uz in the lab frame. The rotation axis is , and the rotation angle is . Using the same axis uaxis(t) and angle ω(t), we then rotate the displacement vector s(Δt) to a new vector s′(Δt). The projections of s′(Δt) to the x-axis and y-axis are and , as illustrated in Figure 2d. The body-frame displacement s⊥(t) perpendicular to the nanorod axis is obtained by summing over and in successive time intervals, i.e., . The normal component of MSD . The diffusion coefficient D⊥ perpendicular to the nanorod axis is determined as the long-time limit of .
The accuracy of the decomposition depends on the time interval Δt. The angle Δθ = cos−1 [u(t) · u(t + Δt)] for the rotation of the nanorod during the time interval Δt needs to be small enough. As shown in Figures S4 and S5, the results of decomposition converge for Δθ < 10°. For all results presented, we ensured that Δθ < 10°. The decompositions of the overall displacements in Figures S2 and S3 are shown in Figures S6 and S7, respectively.
2.3. Calculation of DR
The rational diffusion of a nanorod is schematically shown in Figure 1c. To characterize the rotational diffusion, we followed the unit vector u(t) along the nanorod axis as a function of time t. Three representative rotational trajectories of u(t) are shown in Figure 2b. The rotational diffusion coefficient DR is calculated based on the mean-squared angular displacement of nanorods MSAD = 〈|u(t) − u(0)|2〉. In the large-time limit, MSAD = 2[1 − exp(−2DRt)]. MASD curves for the two sets of simulations in Figures S2 and S3 are shown in Figures S8 and S9.
Although the nanorods are well dispersed and well separated from each other in our simulations, the long-range hydrodynamic effect may affect the diffusion coefficients of nanorods. For a single spherical nanoparticle that is larger than the fluid molecules, the translational diffusion coefficient DT(L) in a finite simulation box of size L is affected by the long-range hydrodynamics, and a term −2.837kBT/6πηL, where η is the bulk viscosity of the fluid, has been used to correct the long-range hydrodynamic effect.44–46 For multiple rod-like nanoparticles in the present simulations, no numerical expressions correcting the long-range hydrodynamic effect exist. A systematic study to determine the correction terms for various diffusion coefficients of the nanorods with different rod lengths in different chain lengths requires extensive computational resources and is beyond the scope of the current study.
3. Results and Discussion
3.1. Diffusion of Nanorods in Unentangled Polymer Melts
We first consider nanorod diffusion in three unentangled melts with N =16, 32 and 64, all of which are below the entanglement length Ne = 85 for kθ = 0. Results for the translational diffusion of nanorods are presented in Figure 3. Simulations allow us to separately obtain DT, D∥, and D⊥ from their respective mean square displacements (MSDs) as functions of time (see Section 2 in SI for the MSDs). All three diffusion coefficients in Figure 3a–c generally decrease with increasing l as nanorods experience more drag from the surrounding polymers. D∥ decreases linearly with increasing l in melts of N = 16, 32, and 64. Solid lines in Figure 3b show the best fits to D∥ = D0(l/σ)−1, where D0 is the monomeric diffusion coefficient for l/σ = 1. According to the Einstein relation, the parallel friction coefficient ζ∥ = kBT/D∥ increases linearly with l. Each of the l/σ beads couples to a local region of monomer size and experiences a monomeric friction . This gives rise to .47 Each individual contributes independently to ζ∥ as the hydrodynamic interactions between different beads are screened. In contrast, the hydrodynamic interactions are not screened in the melts of shorter chains with N = 2, 4, and 8 and in the LJ fluid (N = 1). As shown in the inset to Figure 3(b), D∥l increases with l rather than being constant for N ≤ 8, indicating that the unscreened hydrodynamic interactions reduce the friction with respect to . The focus of this paper is the systems of N ≥ 16.
The cross-section of the nanorod depends upon the direction of its motion, which produces qualitative differences in the diffusion normal and parallel to the rod axis. D⊥ is significantly smaller than D∥ and initially decreases unexpectedly as D⊥ ~ l−2 before crossing over to D⊥ ~ l−1 as l increases. As shown in Figure 3c, D⊥ for N ≥ 16 can be fit with the function , where is the diffusion coefficient at the crossover rod length . A good collapse of the simulation data rescaled by the best-fit values of and is shown in the inset to Figure 3c. The first regime D⊥ ~ l−2 indicates a progressive coupling of nanorods to longer chain segments and eventually the entire polymer chains as l increases. This can be seen by noting that D⊥ ~ l−2 implies that the perpendicular friction per unit length grows linearly with increasing l. The second regime D⊥ ~ l−1 indicates a saturation of the perpendicular friction per unit length for sufficiently large l.
We can compare the diffusion normal to the rod axis and that of a spherical nanoparticle in the same unentangled polymer melts. Scaling theories31,48 show that the friction coefficient of a spherical particle increases from the monomeric friction ζ0 for d comparable to the monomer size b as ζ ≈ ζ0(d/b)3 until d is comparable to the melt chain size R. As d exceeds R, ζ is given by the Stokes’ law ζ = fηmeltd, where f is a numerical prefactor and ηmelt is the bulk melt viscosity. Our simulations reveal ζ⊥ ~ l2 for a nanorod in the first regime. This differs from ζ ~ l3 of a sphere with similar d ≈ l < R, indicating that the shape plays a role in the dynamical coupling of anisotropic nanoparticles and polymer melts, which needs to be included in a theoretical description.49 ζ⊥ ~ l of a nanorod in the second regime is reminiscent of ζ ~ l of a sphere with d ≈ l > R. Previous theory for rod-like colloidal particles of length and diameter in a viscous fluid of viscosity ηs shows that with the logarithmic term correcting for the unscreened hydrodynamic interactions among different sections of the rod.27 There is currently no theory relating ζ⊥ to ηmelt for a nanorod in a polymer melt with the hydrodynamic interactions “partially” screened as in the simulations of N ≥ 16. Numerically, ζ⊥ = (2.7 ± 0.1)ηmeltl for l = 32 in the melts of N = 16 with kθ/ϵ = 0, 1.5, and 3 (see Section 4 in SI for the values of ηmelt).
The total translational diffusion DT is dominated by the motion along the rod axis as l increases. The diffusion anisotropy κ = D∥/D⊥ is shown in Figure 3d. κ first increases linearly with l because κ = ζ⊥/ζ∥ ~ l2/l ~ l. For N = 16, κ eventually levels off as both D∥ and D⊥ scale as l−1 for sufficiently large l. For N = 32 and N = 64, κ has not completely leveled off, as D⊥ ~ l−1 has not fully developed at l = 32σ. Solid lines in Figure 3d are the best fits to , where κc is the diffusion anisotropy at the crossover rod length . The fundamental reason for the diffusion anisotropy is that while the parallel component is coupled only to surrounding monomers, the normal component is progressively coupled to larger chain segments and eventually entire polymer chains with increasing l. κ = 2 in the continuum theory for rod-like colloidal particles as both parallel and perpendicular components of the diffusion experience the same viscosity ηs.27 κ at saturation for monomerically thin nanorods in an unentangled polymer melt can be much larger than 2 and is controlled by ηmelt, which determines ζ⊥ as κ saturates.
Nanorods also undergo rotational diffusion that couples the parallel and perpendicular components of the translational diffusion in their body frame. Understanding how this coupling is related to nanoparticle shape is essential for extracting accurate diffusion data from micro and nanorheology experiments.50 Results for DR of the rods in unentangled melts are shown in Figure 4a. DR shows a strong decrease with increasing l. This is illustrated in Figure 2b, which shows the rotational trajectories swept by several rods of different l over the same time period. In all systems, the decrease of DR exhibits a crossover from DR ~ l−4 to DR ~ l−3, which can be fit by a crossover function , where is the diffusion coefficient at the crossover rod length . The inset to Figure 4a shows that the simulation data collapse when rescaled by the best-fit values of and for different N. The scaling behavior observed for DR is related to that of D⊥ as DR ≈ D⊥l−2.27 Therefore, the crossover from DR ~ l−4 to DR ~ l−3 corresponds to the crossover from D⊥ ~ l−2 to D⊥ ~ l−1, and is a consequence of the progressive coupling to the polymer matrix.
The crossover rod lengths , and all correspond to the rod length above which the nanorods are coupled to the entire polymer chains. As a result, one would expect they are controlled by the polymer chain size. We compare , , and the root mean squared end-to-end size Ree of polymer chains for N = 16, 32, and 64 in Figure S10 of SI. The crossover rod lengths and average polymer size all increase with N, but they are not related by constant numerical factors. What determines the crossover rod lengths is an open question that needs further study.
The rotational diffusion time τR = 1/2DR for the nanorods in chains of N = 64 are indicated by cross symbols on the lines of in Figure 4b, where is the MSD of nanorods normal to the rod axis in the body frame. The plateau of indicates the diffusive regime, with the onset of the plateau corresponding to the translational diffusion time τT in the body frame.51 For l ≤ 8σ, τR precedes the plateau. As a result, rotation of the rod accompanies each diffusion time step in the body frame and couples the orthogonal components. based on independent D∥ and D⊥ over-predicts DT in the lab frame, as shown in the inset to Figure 4b. For l ≥ 16σ, τR is on the plateau. There is no significant rotation for each diffusion time step in the body frame. Therefore, the body and lab frames are equivalent at the diffusion time scale τT, and is valid for l ≥ 16σ.
3.2. Diffusion of Nanorods in Entangled Polymer Melts
As the polymer chain length N increases above the entanglement length Ne, the polymer entanglement network affects diffusion of the nanorods longer than the network mesh size a. Figure 5 shows D∥, D⊥, κ, and DR as functions of l for nanorods in polymer melts with kθ = 1.5ϵ. The entanglement length is reduced to Ne = 28 for kθ = 1.5ϵ.52 Note that kθ = 0 and Ne = 85 for the simulations of unentangled systems in Section 3.1. The polymer melts with N = 16, 100, 400, and 2000 in this section correspond to Z = N/Ne = 0.6, 3.6, 14, and 71, respectively.
The linear decrease of D∥ with l is not affected by the presence of an entanglement network, since the diameter of the rod σ is smaller than the network mesh size a ≈ 5σ. Solid lines in Figure 5a are best fits to D∥ = D0(l/σ)−1. In contrast, D⊥ is suppressed as l grows larger than a. Figure 5b shows that D⊥ ~ l−2 for l ≤ 8σ in entangled chains with N ≥ 100 (Z ≥ 4) is unchanged from the first scaling regime D⊥ ~ l−2 in unentangled chains. While there is a crossover to D⊥ ~ l−1 in the unentangled melt of N = 16 (see the red solid line in Figure 5b), the entangled systems exhibit a steeper decrease in D⊥ for l ≥ 16σ. Figure 2a illustrates the suppression of perpendicular diffusion for the rods of l = 32σ in the entangled melt of N = 400. To describe the motion of a nanorod trapped in an entanglement network, de Gennes developed a rod “reptation” model,53 as schematically illustrated in Figure 1d. In his model, as the rod reptates over a distance of its length l with DT ≈ D∥, the displacement due to normal diffusion ≈ a. From l2/D∥ ≈ a2/D⊥, D⊥ ≈ D∥(a/l)2 ~ l−3. As shown by the black solid line in Figure 5b, D⊥ for N = 400 can be fit to the crossover function , indicating that D⊥ ~ l−3 for l sufficiently larger than a in agreement with de Gennes’ reptation model. Figure 5c shows the suppression of D⊥ enhances κ, which no longer plateaus as in unentangled polymers (red solid line), but instead grows as l2 for large l. The black solid line in Figure 5c is the best fit of κ for N = 400 to the crossover function . κ ~ l2 as D⊥ is reduced by a factor ≈ (l/a)2 compared to D∥. This large ratio means the diffusion of nanorods is dominated by the motion parallel to the rod axis, which only depends on the local dynamics of polymer segments. This result agrees with the experimental observation by Choi et al that the dynamics of nanorods is decoupled from the macroscopic viscosity of polymer melts and thus is only coupled to the local dynamics.20 As the rod diameter goes above a, one would expect a suppression of the parallel diffusion as well. The diffusion of the fat nanorod would rely on the relaxation of the surrounding entanglement network as in the diffusion of a spherical particle with d > a in an entangled polymer melt.32,54,55
The rotational diffusion also exhibits a suppression as l is sufficiently larger than a. Rather than crossing over from DR ~ l−4 to DR ~ l−3, DR in entangled polymers transitions to DR ≈ D⊥l−2 ~ l−5. DR for N = 400 in Figure 5d can be fit to the crossover function . The suppression clearly distinguishes the rotational trajectory of a rod of l = 32σ in the chains of N = 400, as shown in Figure 2b.
The crossover rod lengths , , for N = 400 in Figure 5 all correspond to the rod length above which nanorods are affected by the entanglement network. The crossover rod lengths are expected to be controlled by the network mesh size. As shown in Section 3.2 of SI, , , and , suggesting that the rod length needs to be multiple a for the suppression of nanorod motion.
Using MD simulations, Karatrantos et al.21 have shown that thin nanorods in polymer melts can diffuse faster than predicted by the continuum theory and the diffusion coefficient reaches a plateau as melt chain length N increases, both of which were attributed to local viscosity experienced by nanorods. The N-dependency of the diffusion of thin nanorods in polymer melts has also been examined in the simulations by Li et al.29 The N-dependent transnational diffusion in unentangled melts and N-independent translational diffusion in entangled melts in their simulations were related to the difference between the diffusion parallel and perpendicular to the rod axis. In this work, by decomposing the diffusion into parallel and perpendicular components, we explicitly show thin nanorods only experience monomeric friction for the diffusion parallel to the rod axis and the parallel component D∥ dominates the overall diffusivity, which is the origin of the breakdown of the continuum theory. These findings are consistent with previous simulations.21,29 Furthermore, by identifying the scaling of various diffusion coefficients D∥, D⊥ and DR with rod length l, we elucidate the length-scale dependent coupling of nanorod dynamics to the polymer melts.
For spherical nanoparticles in polymer melts, the dynamical coupling between the nanoparticles and polymers has been described through extending the Stokes-Einstein relation DSE = kBT/ζ = kBT/3πηd for a particle of diameter d in a medium of viscosity η. The essential part of the extension involves a replacement of the bulk viscosity η by an effective viscosity ηeff that depends on the nanoparticle diameter d.31,54,55 Since the bulk viscosity is related to the stress relaxation modulus G(t) of polymer dynamics as , ηeff < η corresponds to a coupling to only part of the polymer dynamics, which can be quantified by an effective relaxation modulus Geff(t). , and Geff(t) for the partial coupling can be obtained from the MSD of nanopartiles by using the generalized Stokes-Einstein relation.35,56–59 For rod-like nanoparticles in polymer melts, the dynamical coupling of nanoparticles and polymers may also be quantitatively described by invoking an effective viscosity ηeff and an effective relaxation modulus Geff(t). Specifically, ηeff may be introduced as in a recent scaling model of the dynamical coupling in liquid polyelectrolyte coacervates,60 and Geff(t) may be computed as in a recent experimental study that quantifies polymer rheology using a rotational generalized Stokes-Einstein relation.50 In this paper, we focus on reporting the scaling relations for the diffusion coefficients of nanorod, while leaving a detailed examination of ηeff and Geff(t) for future research.
4. Conclusions
To summarize, MD simulations of monomerically thin nanorods in polymer melts show a length-scale dependent coupling of nanorod diffusion and the polymer matrix, which is not resolved in current continuum theories. D∥ ~ l−1 if the melt chains are sufficiently long to screen the hydrodynamic interactions among different sections of a nanorod. In unentangled polymers, there is a crossover from D⊥ ~ l−2 to D⊥ ~ l−1 with increasing l, as the rod is progressively coupled to larger segments of the polymer chains with partially screened hydrodynamic interactions. The diffusion anisotropy κ increases with l linearly and eventually saturates for sufficiently large l. The rotational diffusion coefficient DR ≈ D⊥l−2 and exhibits a crossover from DR ~ l−4 to DR ~ l−3. In entangled polymers, the confinement by the entanglement network results in D⊥ ~ l−3 with κ ~ l2 and DR ~−5 for the nanorods with l sufficiently above a. The suppressed dependence of D⊥ and DR on l agrees with de Gennes’ rod reptation model.53
For diffusion of rod-like particles in Newtonian fluids, numerical expressions for diffusion coefficients have been obtained.28,61–66 It remains challenging to derive diffusion coefficients numerically for nanorods in polymer melts. The scaling relations we identify can serve as a foundation for future development of new theories.67,68 With the absence of an analytical theory, they can also guide the experiments69–74 characterizing the transport of anisotropic nanoparticles in polymer matrices. Although DT is the most experimentally tractable diffusion coefficient,69,71 we hope that experimentalists would be motivated by this work to study D∥, D⊥ and DR.
Our findings can provide insights for rod-like nano-objects diffusing in both synthetic gels75 and their biological counterparts.22,23,25 The microscopic picture established here can also benefit the preparation of carbon nanotube-polymer composites,76 green polymer nanocomposites based on rod-like cellulose nanocrystals77 and the understanding of how rod-like virus nanoparticles such as the tobacco mosaic virus transport in polymer solutions.78,79
Supplementary Material
Acknowledgement
We thank Christian Aponte-Rivera for stimulating discussion and comments on the manuscript. T. Ge acknowledges start-up funds from the University of South Carolina. This work was supported in part by the National Science Foundation EPSCoR Program under NSF Award No. OIA-1655740. Any Opinions, findings and conclusions or recommendations expressed in this material are those of the authors and do not necessarily reflect those of the National Science Foundation. Y. Zheng is grateful to the Visiting International Student Program funded by Duke University and Wuhan University. M. Rubinstein acknowledges the financial support from the National Science Foundation under grant EFMA-1830957 and the National Institutes of Health under grant P01-HL108808. Computational resources were provided by University of South Carolina flagship computing cluster Hyperion. This research used resources at the National Energy Research Scientific Computing Center (NERSC), a U.S. Department of Energy Office of Science User Facility operated under Contract No. DE-AC02-05CH11231 and at the Oak Ridge Leadership Computing Facility at the Oak Ridge National Laboratory, which is supported by the Office of Science of the U.S. Department of Energy under Contract No. DE-AC05-00OR22725. These resources were obtained through the Advanced Scientific Computing Research (ASCR) Leadership Computing Challenge (ALCC). This work was performed, in part, at the Center for Integrated Nanotechnologies, an Office of Science User Facility operated for the U.S. Department of Energy (DOE) Office of Science. Sandia National Laboratories is a multimission laboratory managed and operated by National Technology & Engineering Solutions of Sandia, LLC, a wholly owned subsidiary of Honeywell International, Inc., for the U.S. DOEs National Nuclear Security Administration under Contract No. DE-NA-0003525. The views expressed in the paper do not necessarily represent the views of the U.S. DOE or the United States Government.
Footnotes
Supporting Information Available
Parameters for simulation systems, Rg of nanorods, MSD and MSAD of nanorods, fitting results, melt viscosity
The authors declare no competing financial interest.
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