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In the imposed free-draining polymer friction model, the drag coefficients of the $N$ monomers add, giving ${\zeta }_1=N(6\pi \eta a)$ and $D_1=k_{B}T/(6\pi \eta aN)$. Taking the same three-dimensional centre-of-mass RMS convention as part (ii),The polymer is a one-dimensional connected contour, but that alone does not restrict its centre of mass to one spatial axis. If the intended coordinate is instead literal one-dimensional curvilinear motion along an entanglement tube, its RMS contour displacement is $\sqrt{2D_{1}t}=\sqrt{k_{B}Tt/(3\pi \eta aN)}$. That is a different coordinate and should not be compared with a three-dimensional displacement without stating the conversion/model.

Additive local drag is the free-draining Rouse model approximation. It neglects long-range solvent-mediated hydrodynamic interactions and is not a complete theory of an entangled chain. In a tube/reptation description, curvilinear diffusion can scale as $N^{-1}$ while long-time spatial centre-of-mass diffusion scales as $N^{-2}$ after the chain renews its tube. Conversely a dilute unentangled coil can exhibit Zimm model hydrodynamic coupling. Monomer motion, centre-of-mass motion and contour sliding therefore cannot all be identified with the same displacement law.

For the stipulated effective-sphere polymer drag, the radius is the end-to-end RMS distance, $R=2a\sqrt{N}$, rather than the single-monomer radius. Its Stokes law and translational diffusion coefficient areUnder the same three-dimensional RMS convention as used above,Thus for sufficiently long chains ($N>4$), this model gives a larger displacement than independent monomer drag: solvent motion couples the parts of a coil, reducing its effective friction relative to $N$ isolated moving beads. The $D\propto N^{-1/2}$ theta-solvent scaling is consistent with the dilute-coil hydrodynamic scaling underlying the Zimm model, but treating a permeable fluctuating coil as a solid sphere with radius exactly $R_{\mathrm{rms}}$ gives only an order-one hydrodynamic approximation. The hydrodynamic radius and end-to-end radius are not generally equal. Neither model by itself restores the long-time constraints of a truly entangled solution.

If the one-dimensional contour statistic in part (iii) is used literally, the comparison of this three-dimensional $d_2$ with that contour RMS is $\sqrt{3/2}{N}^{1/4}$; it compares different coordinates. Using mean radial displacements in both three-dimensional models instead changes both prefactors equally and leaves their ratio unchanged.

In a dilute solution, solvent-mediated hydrodynamic interactions couple distant chain segments. The Zimm model describes the resulting cooperative dynamics: an intermediate-time segment mean-square displacement scales as $t^{2/3}$, while whole-chain translation has $D_Z\sim k_{B}T/({\eta }_{s}R)$. Once internal modes relax, each tagged segment follows the chain's ordinary long-time diffusion, with mean-square displacement asymptotic to $6D_{Z}t$.

In a concentrated solution or polymer melt, hydrodynamic coupling is screened. The unentangled Rouse model has an intermediate $t^{1/2}$ segment regime and whole-chain diffusivity proportional to $N^{-1}$. Long chains with polymer entanglement are additionally confined by neighbouring chains: reptation gives a slower intermediate $t^{1/4}$ regime and an asymptotic chain diffusivity scaling approximately as $N^{-2}$. The time windows depend on segment, entanglement and terminal relaxation times, so these powers do not all describe the same time interval.

After sufficiently long times both dilute and concentrated chains undergo ordinary translational diffusion. The main long-time difference is the coefficient and its chain-length dependence, with entanglement strongly reducing mobility when the chains are long enough; concentration alone does not guarantee an entangled regime.

In a dilute solution, separate coils diffuse through solvent with long-ranged hydrodynamic coupling among their segments. The Zimm model gives whole-chain diffusionwhere $R_H$ is a hydrodynamic radius and ${\eta }_s$ the solvent viscosity. The coil continually changes shape while its centre of mass performs long-time Brownian motion; treating it as a rigid sphere is only a scaling analogy.

At high concentration, solvent-mediated hydrodynamic interactions are screened on sufficiently large scales and times. If chains are not entangled, additive local or blob friction gives Rouse model behaviour, $D\propto N^{-1}$ at fixed concentration. For long entangled chains, neighboring chains prevent rapid transverse escape. In the reptation tube picture the chain moves mainly along its contour until it renews the surrounding tube. Contour diffusion scales as $N^{-1}$, the tube-renewal time as $N^3$, and the random-coil size squared as $N$. ThereforeBoth cases ultimately give diffusive centre-of-mass motion, but entangled concentrated chains move much more slowly and retain constraints for longer. The inequality $\varphi \gg {\varphi }^{\ast }$ establishes strong overlap, not by itself entanglement: the latter also requires sufficiently many segments relative to an entanglement length. No numerical entanglement scale or concentrated-solution diffusion coefficient is supplied, so only the conditional regimes and scaling exponents can be fixed here.