Shear banding in entangled polymers in the micron scale gap: a confocal-rheoscopic study

Recent shear experiments in well-entangled polymer solutions demonstrated that interfacial wall slip is the only source of shear rate loss and there is no evidence of shear banding in the micron scale gap. In this work, we experimentally elucidate how molecular parameters such as slip length, b, influence shear inhomogeneity of entangled polybutadiene (PBD) solutions during shear in a small gap H ∼ 50 μm. Simultaneous rheometric and velocimetric measurements are performed on two PBD solutions with the same level of entanglements (Z = 54) in two PBD solvents with molecular weights of 1.5 kg mol(-1) and 10 kg mol(-1) that possess different levels of shear inhomogeneity (2bmax/H = 17 and 240). For the PBD solution made with a low molecular weight PBD solvent of 1.5 kg mol(-1), wall slip is the dominant response within the accessible range of the shear rate, i.e., up to the nominal Weissenberg number (Wi) as high as 290. On the other hand, wall slip is minimized using a high molecular-weight PBD solvent of 10 kg mol(-1) so that bulk shear banding is observed to take place in the steady state for Wi > 100. Finally, these findings and previous results are in good agreement with our recently proposed phase diagram in the parameter space of apparent Wi versus 2bmax/H suggesting that shear banding develops across the micron scale gap when the imposed Wi exceeds 2bmax/H [Wang et al., Macromolecules, 2011, 44, 183].


Introduction
Polymeric materials including DNA, actin filaments, plastics, textiles, rubbers and elastomers have emerged as a prominent class of soft matter, which can be found everywhere in nature and industry. 1Long macromolecules can be entangled in their disordered liquid state and display remarkable viscoelastic properties. 2,3Their sluggish macroscopic relaxation arises from chain uncrossability that constrains chains to perform ''reptation'' 4 in the curvilinear one directional tube in quiescence. 5,6Under large fast deformation (when the deformation rate exceeds the reciprocal of the reptation time), the intertwining chains pull on each other, resulting in molecular deformation, until the point of force imbalance, leading to chain disentanglement and yielding of the entanglement network. 7Whether chain disentanglement during large deformation produces a uniform shear field or not is a key issue in the nonlinear rheology of polymers.
Experimental knowledge about nonlinear rheological behavior of entangled polymers typically derives from a rotational shear rheometer where the sample thickness, H, is in the range of 1 mm.Recent experiments combined traditional rheometric measurements with particle-tracking velocimetric (PTV) characterization to obtain more insightful information about how chain entanglement responds to startup shear.At a high Weissenberg number Wi = _ gt 4 1, defined as the product of the bulk shear rate _ g and the longest relaxation (or reptation) time t, many entangled fluids exhibit wall slip and shear banding, including wormlike micelles, 8-12 polybutadiene (PBD), [13][14][15] polyacrylamide, 16,17 DNA, [18][19][20] and F-actin solutions, 21 as well as polymer melts such as styrene-butadiene 22 and polyethylene-oxide. 23On the other hand, such shear banding can be avoided by replacing the sudden startup with gradual ramping up of the applied shear rate. 24,25Moreover, shear banding and wall slip need not occur when the system is insufficiently entangled (the level of entanglements per chain Z o 40) 14,26,27 or has a negligibly small extrapolation length b relative to the sample thickness H, i.e., when b/H { 1. 14,28,29 Recent velocimetric measurements based on the confocal microscopy asserted that there was no bulk shear banding in entangled PBD solutions when the gap of the shear cell is reduced to tens of microns: 30,31 Wall slip was the only discernible form of shear inhomogeneity, with linear velocity profiles across the gap for a high level of entanglement, i.e., Z = 56 entanglements per chain.Such results were used to suggest that the previously observed shear banding 13,14 involving a conventional cone-plate or a parallel-disk device was due to the edge fracture: the absence of shear banding in a shear cell with a gap distance much lower than the conventional gap (e.g., by a factor of 20) was assumed to be due to the fact that there is a negligible effect of edge fracture in the shear cell with a 50 mm gap.
Wall slip is a well-established phenomenon in both polymer melts and solutions. 32During startup shear with Wi 4 1, entangled polymers show the first sign of shear inhomogeneity in the form of wall slip by interfacial disentanglement, because the polymer/wall interface is weaker than the cohesion of entangled networks. 33The intrinsic ability of the entangled solution to undergo slip can be estimated in terms of the slip length b.The magnitude of b B (Z/Z i )a relative to the sample thickness H determines how much the actual bulk shear rate _ g b is reduced from the nominal rate _ g, 19,29 where a is the interfacial layer thickness, Z and Z i are the bulk and interfacial viscosities respectively.The maximum value of b, denoted as b max , corresponds to the full interfacial disentanglement when Z i reduces to the solvent viscosity Z s , i.e., b max = (Z/Z s )a(f).For polymer solutions, a would grow from its value in the melt l ent upon dilution as: a(f) = l ent f À0.66 , where f is the polymer volume fraction.
Upon startup shear with Wi 4 1, wall slip will emerge as a consequence of interfacial yielding. 29,33Denoting the effective shear rate in the bulk as _ g b , then the speed of the shearing wall is given in terms of the slip velocity V s as which can be rewritten as where the nominal rate _ g = V/H and the slip length b has its kinematic meaning according to b = V s /_ g b , which is illustrated in Fig. 1.With increasing V or _ g, V s and b grow towards their maximum values.Before the maximum slip velocity is reached, the bulk shear rate _ g b can be expected to remain at a critically low value around 1/t. Correspondingly, the steady-shear stress does not appreciably increase with _ g.In other words, the value of _ g can increase up to _ g wb-bnl = (1 + 2b max /H)/t without forcing the bulk to leave the Newtonian regime whose upper-bound is given as 1/t.
In other words, there is a critical Weissenberg number Wi ws-bnl , beyond which the bulk starts to enter the nonlinear response regime, given by Wi ws-bnl = (1 + 2b max /H) ( When Wi 4 Wi ws-bnl , even maximum wall slip cannot save the bulk from having Wi b = _ g b t > 1.Here the subscript ''ws-bnl'' stands for a transition from wall slip (ws) to bulk nonlinear response (bnl).For well-entangled polymer solutions, Wi ws-bnl can be very large when H is reduced from a conventional gap distance of 1 mm to 50 mm.This is a reason why Hayes et al.only reported wall slip as the source of shear rate loss for entangled PBD solutions. 30n passing, we also note that the maximum value of b max corresponds to the slip velocity V s attaining its maximum at Wi ws-bnl where the bulk shear rate _ g b B t À1 .Thus, we have In the current study, we show that the dominant wall slip characteristic of the previous reports 30,31 is replaced by bulk shear banding when the extrapolation length b is reduced using a polymeric solvent of sufficient high molecular weight.Specifically, one of our two 13 wt% PBD solutions shows only wall slip, similar to one solution reported previously, 30,31 because of its high value for b max , whereas the second solution displays bulk shear banding because of its lower value for b max .Because the point of velocimetric observation in our setup is at least 3 mm away from the meniscus in a parallel-disk shear cell with H B 50 mm, the aspect ratio is 60, no edge fracture and sample loss took place during shear.Finally, our findings in the micron scale gap are presented in terms of a phase diagram in the parameter space of apparent Wi versus 2b max /H.We demonstrate that b max is a key parameter for a fixed gap to control what type of velocity profile may occur for a given Wi and bulk shear banding can develop when the applied Wi exceeds 2b max /H.At sufficiently high Wi, the linear velocity profile is recovered across the gap.

Materials and sample preparation
Our experiments are based on two well-entangled 1,4-polybutadiene (PBD) solutions made with the same parent high molecular weight PBD (M w B 10 6 g mol À1 ) at the same 13 wt% concentration in polymeric butadiene (PBD) ''solvents'' (with molecular weights of 1.5 kg mol À1 and 10 kg mol À1 ).In this work, these two solutions are labelled as 1M(13%)1.5Kand 1M(13%)10K.The molecular characteristics of parent polymers and solvents are listed in Table 1.The parent PBD was first dissolved in excess of toluene to which the PBD solvent was added and intimately mixed.For the particle tracking velocimetric (PTV) observations, fluorescein isothiocyanate (FITC) labelled fluorescent melamine micro-beads with a particle size of 1 mm (Sigma Aldrich, CAT no 90305) were dispersed in toluene and then added to the solution with the final loading of the particles around 600-800 ppm.Most of the toluene was evaporated at room temperature under a hood for days, and the remaining was removed by applying vacuum until the residual toluene is less than 0.5%.

Rheometric and velocimetric measurements
In this work, we integrated a Bohlin-CVOR rheometer with a spin-disk confocal microscope to make the particle-tracking velocimetric (PVT) measurements at an unconventionally low gap distance of H = ca.50 mm.The schematic representation of our confocal rheoscope is shown in Fig. 2 that involves an Olympus IX-81 inverted microscope.An EM-CCD camera (Hammamutsa) connected to the CFM was used to take twodimensional (2D) movies in the XY plane through a piezomounted objective lens (60Â, 1.4 NA).The field of view in our measurements is about 100 mm Â 100 mm where the PTV observations are performed at a distance of 3 mm from the meniscus so that the aspect ratio of the distance from the edge to the gap distance is ca.60 (for H = 50 mm).The lateral resolution, axial resolution, and optical slice thickness are 0.2, 0.5, and 1.34 mm, respectively.The camera and spinning disk were synchronized, and the entire system was controlled using VoxCell software from Visitech International.
A custom-made microscope stage was designed so that our rheometer (Bohlin CVOR) could integrate with the stage mounted onto a confocal fluorescence microscope (CFM) with three adjustable screws to ensure alignment.Initially, the adjustable platform allowed us to pre-align the rheometer on an optical table, on which the CFM was placed.The rotating shaft has a short length of 2 cm to ensure good parallelism of the rotating disc to the bottom plate.To verify the alignment, the upper disc was first raised 5 mm above the stationary bottom plate and then spun to detect any misalignment.This setup has been previously employed to accurately conduct molecular imaging of entangled DNA solutions on the micron scale, 34 correlating interfacial slip with conformations of DNA adsorbed at wall.
All startup shear measurements were performed at room temperature around 25 1C, based on parallel-disk geometry with a radius R = 10 mm and H = ca.50 mm.Here all apparent shear rate values in the fluid sample are estimated as _ g = OR/H, where O is the imposed angular velocity at R = 7 mm (at a radial distance of 3 mm from the edge).To determine the linear viscoelastic properties of these two entangled PBD solutions, small amplitude oscillatory shear (SAOS, strain amplitude _ g = 5%) frequency sweep tests were conducted in a conventional parallel-plate shear cell with H = 1 mm.All startup shear tests were performed in the controlled rate mode at a narrow gap (H = ca.50 mm) under the confocal microscope to capture the velocity profiles across the gap.The top and bottom plates were a glass slide (thickness 0.15-0.17mm).The bottom plate was placed on the microscope stage, along with a circular plastic O-ring (inner radius 14 mm) to minimize meniscus instability and sample loss during high shear.The top moving and bottom stationary transparent plates were identified by scanning along the sample thickness direction to confirm that the nominal gap is consistent with the true gap.In all startup shear experiments, 2D images were captured every 2 to 4 microns across the sample thickness (with a rate of 35 to 45 fps) to measure both the transient and steady velocity profile across the gap.Typical error bars in the measured velocity are about 5%, which was achieved by keeping track of sufficiently large displacements of the fluorescent particles.

Extraction of slip velocity, slip length and local shear rates during shear
The experimental understanding of polymer rheology depends on simple shear rheometric measurements.Usually, rheological properties of polymeric fluids are obtained based on the assumption that a uniform shear field with a constant shear rate (_ g = V/H) should prevail across the gap with no slip boundary condition, where V is an imposed (apparent) velocity and H is a sample thickness sandwiched between two parallel plates.
At high shear rates, entangled fluids violate no-slip boundary condition and show strong wall slip during shear.The most effective way to quantify the slip is to introduce the slip length b = V s /_ g b .The magnitude of b relative to the sample thickness H determines how much the actual bulk shear rate _ g b is reduced from the apparent rate _ g.In this work, the slip velocity V s and bulk rate _ g b are directly measured by confocal imaging to estimate the slip length, b, for both solutions.Specifically, to obtain accurate local shear rates, the velocity profiles with high  spatial resolutions were constructed across the gap from PTV.Then, _ g b was evaluated from the velocity profile using ordinary least squares regression.The formation of two or more flow regimes with different local shear rates under the same imposed rate was defined from the best fits.

Conventional rheometric measurements
Fig. 3a shows dynamic storage and loss moduli G 0 and G 00 of the two 13 wt% PBD solutions made with 1.5KPBD and 10KPBD respectively.The linear viscoelastic characteristics of these two samples are listed in Table 2, where the plateau modulus G pl was determined from the value of G 0 at a frequency where G 00 shows a minimum, and the longest relaxation time t is estimated from the inverse of the crossover frequency o c where G 0 = G 00 .The similar value of G pl confirms that the level of chain entanglement is the same in these two PBD solutions.The number of entanglements per chain can be estimated to be around 54 according to Z = (M w /M e )f 1.2 , where M w is the molecular weight of the parent PBD, M e the entanglement molecular weight for PBD melts, taken to be 1600 g mol À1 .The Rouse relaxation time of two solutions is determined to be t R = t/3Z.Given l ent = 3.8 nm, 35 we find a to be ca.15 nm at 13 wt% of 1MPBD.
Table 2 lists Wi ws-bnl for the two polymer solutions by taking H = 50 mm.According to eqn (2), to observe shear banding in the bulk, we need to apply Wi in excess of either 17 or 240 respectively for the two solutions.By choosing two different solvents, we have estimated b max to differ by a factor of ten as listed in Table 2.Here b max is calculated based on the estimated values of Z from Fig. 3.
Next, we performed startup shear experiments to investigate the rheological responses at a narrow gap of H = ca.50 mm in the steady state.Fig. 3b displays the flow curves, showing steady shear stress against the nominal Wi, where the shear rate is given by OR/H, with O the angular velocity, R the disk radius.The two flow curves are very similar, showing the characteristic of stress plateau, both considerably below the curves of |G*| vs. ot.Because the parallel-disc setup was used to make these measurements, Fig. 3b only reflects an approximate shear stress vs.rate relationship.

Homogenous shear in the Newtonian regime (Wi o 1.0)
To check the reliability and performance of our confocal rheoscope, we sheared 1M(13%)1.5K in the terminal regime (Wi o 1.0) where it behaves like a Newtonian liquid.Fig. 4a shows that there is no stress overshoot at a low shear rate _ g = 0.01 s À1 (Wi = 0.36).Under this condition, the velocity profile is uniform across the sample thickness at all times, where the bulk shear rate (_ g b B 0.009 s À1 ) is close to the imposed shear rate as shown in Fig. 4b.Small deviation from the imposed shear rate indicates weak wall slip near both top and bottom plates occurs (V s B 0.03 mm s À1 ).These results are consistent  , where o c (in rad s À1 ) is the crossover frequency in a frequency sweep test.b Entanglement density, Z(f), is calculated by (M w /M e )f 1.2 , where M e = 1600 g mol À1 for 1,4 PBD melts.c Rouse times of two solutions are determined as t R = t/3Z.d The zero shear viscosity of the polymer solutions is estimated from Fig. 3. e Interfacial layer thickness of polymer solutions is estimated to be a(f) = l ent f À0.66 , where l ent = 3.8 nm for pure PBD melts and f is the polymer volume fraction.f The theoretical maximum extrapolation length is estimated to be b max = (Z/Z s )a(f), where Z s for 1.5KPBD and 10KPBD is 0.7 and 14 Pa s respectively.g The critical Weissenberg number is estimated to be Wi ws-bnl = 2b max /H, where H = 50 mm.This journal is © The Royal Society of Chemistry 2015 with previous reports 18,30 of homogenous shear in entangled polymers when Wi o 1.0.At a shear rate of 0.4 s À1 (Wi B 14), the shear stress overshoot occurred during startup shear as shown in Fig. 5a, and the velocity profile is linear around t = 1 s before stress overshoot and displays strong slip after the stress maximum as shown in Fig. 5b.The velocimetric measurement reveals that the bulk of the sample experiences a mere shear rate of 0.03 s À1 , which is comparable to the reciprocal of the terminal relaxation time (t = 36 s).At higher shear rates of 1.6, 3.0 and 8.0 s À1 (Wi = 57-288), apparent wall slip appears to be the only form of shear inhomogeneity near the steady state as shown in Fig. 6a and b.Accessing higher deformation rates (Wi 4 296) to observe bulk shear banding across the gap is infeasible for PBD1M(13%)1.5Kbecause our PTV technique is limited to shear rates up to 10 s À1 .

Shear banding in 1M(13%)10K (100 r Wi r 408)
The intrinsic ability to undergo wall slip can be considerably reduced by using a polymeric solvent with a sufficiently high molecular weight to increase the upper bound for the interfacial viscosity Z i . 29In this section, we only focus on steady-state velocity profiles at different shear rates in the stress plateau region.At a low shear rate _ g = 0.3 s À1 (Wi B 20), this solution also violates the no-slip boundary condition at the top and bottom plates after stress maximum is reached, and strong slip prevails across the gap as shown in Fig. 7a and b.On the other hand, when Wi 4 100, shear banding emerges across the small gap.The growth of shear stress for shear rates of 1.5, 3.0 and 6.0 s À1 during startup shear is plotted in Fig. 8a.Fig. 8b shows that the velocity profile becomes nonlinear, characteristic of shear banding (with three different local shear rates of 0.15, 0.86 and 4.39 s À1 ) in the steady state for a nominal shear rate of 1.5 s À1 .Previous velocimetric measurements on polymer  solutions 14 have also reported the existence of multiple shear banding across the gap.For shear rates of 3.0 and 6.0 s À1 , permanent shear banding persists across the gap even after hundreds of strain units, as shown in Fig. 8c.Accompanying the high shear band is also significant wall slip.For apparent shear rates of 1.5, 3.0 and 6.0 s À1 , the local rate in the high shear band is 4.39, 5.67 and 14.48 s À1 respectively.As a function of the apparent shear rate, the local shear rate varies in each of the low, medium or high band, as shown in Fig. 8d.The local shear rate in the high band seems to increase exponentially with an apparent shear rate.

Normalized steady state velocity profiles: slip vs. shear banding
Fig. 9a and b respectively present the normalized steady-state velocity profiles for the two solutions at different Wi.In Fig. 9a, the 1M(13%)1.5Ksolution shows nothing else but massive slip in the range of Wi from 14 to 288.In contrast, Fig. 9b shows that bulk shear banding develops across the gap in the range of Wi from 102 to 408 for 1M(13%)10K.Fig. 9c displays the steady state velocity profiles at comparable Wi = 288 and 272; _ gt R = 1.8 and 1.7, showing slip and bulk shear banding respectively of the two solutions.
Our PTV measurements allow us to examine how the wall slip grows in magnitude, i.e., how the slip velocity V s increases with the applied rate _ g toward its maximum.According to   is also observed for 1M(13%)10K up to 1.0 o Wi o 20.The slip velocity V s starts to deviate from the linearity for Wi 4 20, confirming that the shear rate _ g b remained unchanged up to Wi = 20.The value V s of 1M(13%)10K stays well below that of 1M(13%)1.5Kfor all values of Wi -noting the different scales used for the double-Y axes.When the increase of V s starts to deviate downward from linear growth with Wi, it has already reached its maximum at 6 mm s À1 , which coincides with the theoretical estimate of eqn (3): V s(max) B b max /t = 420/68 = 6.2 mm s À1 .Because of the poor spatial resolution, the higher of V s observed at high Wi indicates apparent wall slip that involves a slip layer increasingly thicker than one monolayer.Fig. 9e shows the changes in the slip length b = V s /_ g b as a function of Wi for the two solutions.The slip length b ranges from 10 to B1100 mm for 1M(13%)1.5K,which is one order of magnitude higher than slip length of 1M(13%)10K (maximum b B 190 mm).This can be estimated from the information in Table 1 showing that Z s of PBD10K is 20 times as high as that of 1.5KPBD.

Relationship between local and apparent Wi and comparison with previous work
Upon extracting the local, i.e., bulk, Weissenberg numbers from our velocimetric measurements, we show the relationship between the bulk Weissenberg number Wi b and nominal Wi in Fig. 10.Here we compare our findings with the previous work obtained in a narrow-gap to address and discuss why only either linear velocity profile or wall slip was observed in the previous report.Hayes and coworkers 30 studied five different entangled solutions with different volume fractions f based on two high molar mass PBD (M w = 0.7 Â 10 6 g mol À1 , M w /M n = 1.1) and PBD (M w = 0.2 Â 10 6 g mol À1 , M w /M n = 1.05) in an un-entangled PBD1K solvent (M w = 1 Â 10 3 g mol À1 ).These PBD solutions with a wide range of level of entanglements (8 r Z r 56) were reported to show a linear velocity profile with some wall slip.We estimate the rheological properties and slip characteristics of five solutions as shown in Table 3.Among these five solutions, 0.2M(40%)1K, 0.2M(60%)1K and 0.7M(20%)1K have a sufficiently high level of entanglements (32 r Z r 56) capable of producing shear banding across the gap at high values of Wi.We also note that only 0.7M(20%)1K was sheared at sufficiently high Wi (9 r Wi r 114).The two PBD solutions, based on the parent PBD200K named 0.2M(40%)1K and 0.2M(60%)1K, were only explored in the Newtonian regime (0.08 r Wi r 0.7).It is well established that a linear velocity profile should be maintained across the gap when Wi o 1.0.In general, at low shear rates (Wi o 1.0), the nominal and local Weissenberg numbers are the same, which is consistent with previous reports on entangled systems. 18,30Besides, at Wi = 0.7 and 0.5 (closer to Wi = 1), both 0.2M(40%)1K and 0.2M(60%)1K suffered from some degree of wall slip, 30 as denoted by the triangles in Fig. 10.This is expected.
At higher Wi in the non-Newtonian regime (Wi 4 1.0), we see that Wi b remains the order of unity because of the dominant wall slip in 1M(13%)1.5K,except for last two points.In the explored range of apparent shear rates, the solution based on the 1.The lack of wall slip is at odds with their report of wall slip for the other solutions and in disagreement with our findings shown in Fig. 10.When Wi is increased to 113, the velocity profile began to deviate significantly from nominal Wi, displaying shear banding.This response can be consistent with our observation of shear banding, because shear banding should occur for 0.7M(20%)1K when Wi 4 Wi ws-bnl B 80 (see diamonds in Fig. 10).However, Hayes et al. suggested that this behavior could be originated from secondary flows due to chain stretching and normal stresses at a high shear rate.Since most of the reported values of Wi in Hayes et al.'s measurements are less than critical Wi ws-bnl , except for one date point of 0.7M(20%)1K (at Wi = 113), it is expected to observe a linear velocity profile in their measurements.In this work since the point of PTV observation is so far away from the edge, it is implausible for our results to have anything to do with any edge instability.Thus we have proposed localized chain disentanglement as the origin of shear banding, more systematic studies are required to look for   evidence of the secondary flow phenomenon and the effect of edge failure on the bulk velocity profile of well-entangled PBD solutions in such small-gap shear cells.

Suppression of edge effects at a small gap
Edge fracture occurs frequently in well-entangled polymeric systems at high Wi in a conventional rheometric setup (with a gap size of 1 mm). 38,39This phenomenon is attributed to the build-up of normal stresses. 38,40When edge fracture occurs, the sample may ''leak out'' at the meniscus during shear leading to a reduced stress response.It has been reported in the literature that a large decrease of the gap distance can minimize the edge effects during shear of entangled polymer solutions. 30We carry out SAOS to verify whether there is any sample loss during shear banding.Fig. 11 shows that dynamic oscillatory shear data are identical before and after shearing at shear rates of 1.5, 3.0 and 6.0 s À1 .Additionally, it is known that edge fracture would be more severe at high Wi, due to increased normal force.Fig. 12 shows that at higher Wi, a linear velocity profile is actually recovered in the steady state.Specifically, at a sufficiently high shear rate of 8.0 s À1 , the uniform shear is recovered (at t = 77 s) after showing transient inhomogeneity (at t = 7.7 s) across the gap.Therefore, we can conclude that edge fracture has been minimized and sample loss is negligible in our measurements, and our setup can be ideal for studying the non-linear response in entangled polymers at high Wi.

The phase diagram
We can construct a ''phase diagram'' to summarize our findings in terms of Wi versus 2b max /H, as shown in Fig. 13.Clearly, b max is one of the key parameters to highlight when and what type of shear inhomogeneity may occur at different Wi for a fixed gap.For both 0.7M(20%)1K and 1.0M(13%)1.5K,much higher Wi is required to obtain shear banding, due to a high value of slip length.We should emphasize that this phase diagram can only qualitatively describe whether shear banding occurs or not during shear for well-entangled systems (Z 4 40).

Conclusions
In this study, two entangled PBD solutions with the same level of entanglement (Z = 54) have been subjected to various values of nominal shear rate _ g to explore their nonlinear rheological responses in a shear cell with a small gap distance in the 50 micron range.2][43] Using a confocal microscope integrated with a rotational rheometer, we obtain simultaneous global rheology (apparent rheometric measurements) and local velocity profiles.This setup allows us to probe when and what type of shear inhomogeneity (interfacial slip vs. shear banding) occurs across the gap.For the entangled PBD solution made with a low molecular weight PBD (M w = 1.5 kg mol À1 ), only interfacial slip or   apparent wall slip can be observed up to a shear rate of 8 s À1 .In contrast, the second solution, the higher molecular weight PBD (M w = 10 kg mol À1 ) solvent reduces the magnitude of the slip length b so that apart from wall slip bulk shear banding can also take place at the experimentally accessible shear rates.The prevalence of interfacial slip in 1M(13%)1.5K is consistent with the findings of Hayes and coworkers. 30,31On the other hand, 1M(13%)10K exhibits shear banding despite a small gap distance of 50 mm, when imposed Wi exceeds a critical value if Wi, i.e., 2b max /H.Finally, at sufficiently high Wi, shear homogeneity is restored across the gap for 1M(13%)10K.

Fig. 1
Fig. 1 Schematic diagram of the velocity profile within the gap of the shear geometry in the presence of (left) wall slip, where b = V s /_ g b , and (right) bulk shear banding at the apparent shear rate.

Fig. 2
Fig. 2 (left) Schematic illustration of the rheo-confocal setup used for simultaneous rheometric and velocimetric measurements at room temperature with H = ca.50 mm.(right) Sketch of the parallel-disk geometry with three different velocity profiles: uniform flow, slip and shear banding.The velocity profiles were measured by tracking the fluorescent melamine micro-beads with a size of 1 mm.

Fig. 3
Fig.3(a) Small amplitude oscillatory shear (SAOS) measurement of two well-entangled PBD solutions.Dynamic storage, loss moduli and complex viscosity of 1M(13%)1.5Kand 1M(13%)10K as a function of frequency using strain amplitude of 5% at room temperature (geometry: a 20 mm parallel-disk cell with separation of 1 mm).(b) Steady shear stress versus Wi (geometry: a 20 mm parallel disk with a gap distance of ca.50 mm), along with the oscillatory shear data of G* versus the dimensionless oscillation frequency (ot) for two PBD solutions.

Fig. 4
Fig. 4 (a) Shear stress response upon startup shear at a rate of 0.01 s À1 as a function of time.The arrows indicate the moments when the velocity profiles were measured and presented in (b).Linear velocity profiles prevail at different times at such a low shear rate (Wi = 0.36), involving the 20 mm-diameter parallel-disk with a separation of 50 mm.The open circle represents the velocity of the upper plate, not PTV measurement.

Fig. 5
Fig. 5 (a) Shear response upon startup shear at a rate of 0.4 s À1 (Wi = 14) for 1M(13%)1.5K.(b) The evolution of the velocity profile at different times (t = 1, 30 and 75 s).Velocity profile is linear across the gap, before stress maximum then massive slip developed at long times, in the 20 mm-diameter parallel-disk shear cell with a separation of 50 mm.The open circle represents the velocity of the upper plate, not PTV measurement.

Fig. 6
Fig. 6 (a) Shear stress response upon startup shear at different shear rates (_ g: 1.6, 3.0 and 8.0 s À1 ) for 1M(13%)1.5K.(b) The linear velocity profiles in the bulk with strong slip at both surfaces at the moments indicated by the vertical arrows in (a), from the 20 mm-diameter parallel-disk shear cell with a separation of 50 mm (at _ g = 1.6 and 3.0 s À1 ) and 40 mm (at _ g = 8.0 s À1 ).The rheometric velocities of upper plates are represented by open symbols.

Fig. 7
Fig. 7 (a) Shear stress response upon startup shear at a rate of 0.3 s À1 (Wi = 20).(b) Steady-state linear velocity profile with apparent wall slip for 1M(13%)10K when Wi o Wi ws-bnl , obtained from the 20 mm-diameter parallel-disk shear cell with a separation of 50 mm.The open circle represents the velocity of the upper plate, not PTV measurement.

Fig. 8
Fig. 8 (a) Shear stress response upon startup shear at different shear rates (_ g: 1.5, 3.0 and 6.0 s À1 ) for 1M(13%)10K measured from the 20 mm-diameter parallel-disk shear cell with a separation of 50 mm.(b) Shear banded velocity profile with formation of three flow regimes (0.15, 0.86 and 4.39 s À1 ) for an apparent shear rate of 1.5 s À1 in the steady state as indicated by the vertical arrow in (a).(c) Banded velocity profiles of 3.0 and 6.0 s À1 in the steady state as indicated by the vertical arrow in (a).The rheometric velocities of upper plates are represented by open symbols in (b and c).(d) The local shear rates (obtained from PTV measurements) versus apparent shear rates for 1M(13%)10K.

Fig. 9
Fig. 9 Snap shots of velocity profiles in the steady state for (a) 1M(13%)1.5K(slip-like behavior) and (b) 1M(13%)10K (bulk shear banding at 100 r Wi r 408 and uniform shear at Wi = 520).(c) The normalized velocity profiles of the two PBD solutions at Wi = 288 and 272; _ gt R = 1.8 and 1.7, showing slip and shear banding respectively.(d) Slip velocity versus apparent Wi for the two PBD solutions.(e) Estimated slip length, b, versus apparent Wi for the two PBD solutions where the vertical bar indicates the maximum difference.
5 K solvent has b equal to 1100 mm and shows interfacial slip or apparent wall slip only up to Wi = 288 (_ gt R B 1.8).The PBD solution with a PBD10K solvent shows the coexistence of high and low shear bands, along with wall slip because its b = 190 mm.We note that beyond Wi = 100; _ gt R B 0.6, there can be three bands of different local rates in the bulk for 1M(13%)10K.In contrast, a linear velocity profile without wall slip was reported by Hayes et al. for their 0.7M(20%)1K (Z B 51) till Wi = 45.

Fig. 10
Fig. 10 Local Wi b against apparent Wi for five PBD solutions with a sufficiently high level of entanglements (32 r Z r 56).Diamonds and triangles are extracted from the work of Hayes et al.Both 0.2M(40%)1K and 0.2M(60%) were only sheared at a low shear rate such that Wi o 1.0 (highlighted by the dashed box in the Newtonian regime).At high Wi 4 100, the coexistence of high and low Wi b appears across the micron scale gap for 1M(13%)10K, in contrast with apparent slip of 1M(13%)1.5Kthat keeps Wi b low as indicated by the circles.For 0.7M(20%)1K, the coexistence of a high and a low shear band has been reported by Hayes et al. at Wi = 113.Note that values of Wi ws-bnl for 1M(13%)1.5K,1M(13%)10K, and 0.7M(20%) are highlighted by vertical blue, red and black arrows respectively.

a
) d (kPa s) a(f) (nm) b max = (Z/Z s )a(f) e (mm) Wi ws-bnl B 2b max /H f Plateau modulus of PBD samples was provided in PhD thesis of Keesha Hayes. 36b Z(f) is estimated by (M w /M e )f 1.2 , where M e = 1600 g mol À1 for 1,4 PBD melts.c Z(f) is reported by Hayes et al., where M e is assumed to be around 2000 g mol À1 .d Bulk shear viscosity of polymer solutions is estimated to be Z ¼ p 2 12 G pl t. 5 e Maximum extrapolation length is estimated, where solvent viscosity (PBD1K, M n B 1000 g mol À1 , Aldrich Inc.) is assumed to be around 4.0 Pas at room temperature. 37The vinyl content of PBD1K (Aldrich 200417) is higher than PBD1.5K(Aldrich 200484) leading to lower T g and higher viscosity.f Wi ws-bnl is estimated, where H = 35 mm.This journal is © The Royal Society of Chemistry 2015 Soft 2015, 11, 8058--8068 | 8067

Fig. 11
Fig.11Small amplitude oscillatory shear (SAOS) measurements before and after shear rates (with 650 s rest time for entanglement recovery after applying steady shear rates).Dynamic storage (closed symbols) and loss (open symbols) moduli of 1M(13%)10K as a function of frequency using strain amplitude of 5% at room temperature.

Fig. 12
Fig. 12 Restoration of the uniform velocity profile at a high shear rate.Characterization of the velocity profile at high shear rates = 8.0 s À1 (Wi = 544) at t = 7.7 and 77 s.The inset shows a shear stress response upon startup shear at a rate of 8.0 s À1 .

Fig. 13
Fig. 13 Phase diagram in the parameter space of apparent Wi versus 2b max /H for our findings at a small gap for PBD solutions (Z = 54) in different PBD solvents.

Table 1
Molecular characteristics of parent 1MPBD, and 1.5KPBD and 10KPBD solvents

Table 2
Linear viscoelastic properties and slip characteristics a Terminal relaxation times are estimated as t = o c À1 Fig.9dplots V s against Wi for both PBD solutions.With increasing Wi, the value of V s grows linearly for 1M(13%)1.5K.Similar behavior s would change linearly with Wi as Wi = (V/H)t = 2V s /(H/t) + t_ g b if the bulk rate _ g b were to remain little changed with Wi. 18,29

Table 3
30mposition and linear rheological properties of PBD solutions reported in the work of Hayes et al.30