Depletion and the Dynamics in Colloid–Polymer Mixtures

Depletion and the Dynamics in Colloid–Polymer Mixtures

Current Opinion in Colloid & Interface Science 20 (2015) 66–70 Contents lists available at ScienceDirect Current Opinion in Colloid & Interface Science journal homepage: www.elsevier.com/locate/cocis Depletion and the dynamics in colloid–polymer mixtures Remco Tuinier a,b,⁎, Tai-Hsi Fan c, Takashi Taniguchi d a Van't Hoff Laboratory for Physical and Colloid Chemistry, Department of Chemistry, Debye Institute, Utrecht University, Padualaan 8, 3584 CH Utrecht, the Netherlands b DSM ChemTech R&D, Advanced Chemical Engineering Solutions (ACES), P.O. Box 18, 6160 MD Geleen, the Netherlands c Department of Mechanical Engineering, University of Connecticut, CT 06269, USA d Graduate School of Engineering, Kyoto University, Katsura Campus, Nishikyo-ku, Kyoto 615-8510, Japan article info abstract Article history: The status of work on the influence of nonadsorbing polymers on depletion dynamics in colloidal dispersions is Received 3 November 2014 reviewed. In the past focus has been paid to equilibrium properties of colloid–polymer mixtures. In practice the Accepted 26 November 2014 dynamical behaviour is equally important. Dynamic properties including colloid diffusion, sedimentation and Available online 11 December 2014 suspension rheology as affected by polymer-induced depletion attraction are discussed. © 2014 Elsevier Ltd. All rights reserved. Keywords: Depletion interaction Colloidal dynamics Polymers Slip Diffusion Sedimentation 1. Introduction [4–6], and these are highly relevant for understanding suspensions con- taining colloidal particles plus nonadsorbing polymers. Phase transition Colloid–polymer mixtures have gained increasing attention since phenomena have drawn quite some attention [7,8]. The demixing the 1980s for both practical and fundamental reasons. In many industri- process of an unstable colloid–polymer mixture can proceed in several al products such as food [1], and paint [2], polymers and colloids are ways. Both spinodal decomposition [9–11] as well as nucleation and mixed together so studies on colloid–polymer mixtures are very helpful growth coarsening can take place. for giving insight into for instance the conditions that keep the mixtures Before reviewing the dynamics, the key aspects of equilibrium stable. Fundamentally, it is understood that adding nonadsorbing properties in colloid–polymer mixtures are briefly summarized. Adding polymers to a colloidal dispersion allows tuning the range and strength non-adsorbing polymers to a dispersion of colloidal spheres effectively of the attractive pair interactions and alters the colligative properties of induces attractive forces between them [3]. The attraction originates colloidal mixtures. In practice however the nonequilibrium behaviour from the presence of depletion zones around the colloidal spheres, 3 is at least as important. In this review we focus on the dynamics of each having a volume vc =4πa /3, with sphere radius a. The depletion relatively dilute and stable colloidal dispersions. zone results from a loss of conformational entropy of the polymer In contrast to equilibrium properties of colloid–polymer mixtures chains close to the surface of the colloidal particles. Overlap of depletion set by thermodynamics [3], there are relatively few investigations on zones causes an inhomogeneous osmotic pressure distribution by the dynamics that couples Brownian motion, hydrodynamic interaction, polymers around the neighbouring particles, first understood by polymer transport and microstructure evolution in colloid–polymer Asakura and Oosawa [12].TheAsakura–Oosawa–Vrij (AOV) expression mixtures. Dynamical properties such as diffusion, sedimentation, and for the depletion interaction [12,13] between two colloidal hard suspension rheology have been studied in well-defined colloidal spheres, each surrounded by a depletion layer with thickness δ is: (hard-sphere and adhesive hard-sphere) suspensions in great detail 8 < ∞ rb2a ðÞ¼ −Π ðÞ ≤ ≤ ðÞþ δ : ð Þ Wr : V ov r 2a r 2 a 1 0 r N2ðÞa þ δ ⁎ Corresponding author at: Van't Hoff Laboratory for Physical and Colloid Chemistry, The osmotic pressure of the polymer solution Π depends on the Department of Chemistry, Debye Institute, Utrecht University, Padualaan 8, 3584 CH Utrecht, the Netherlands. polymer concentration c and can, for ideal (non-self-interacting) 3 E-mail address: [email protected] (R. Tuinier). depletants, be written as Πvcq /kT = c/c* in the case of a dilute polymer http://dx.doi.org/10.1016/j.cocis.2014.11.009 1359-0294/© 2014 Elsevier Ltd. All rights reserved. R. Tuinier et al. / Current Opinion in Colloid & Interface Science 20 (2015) 66–70 67 solution, where q = δ/a and c* is the polymer overlap concentration. φ The interparticle dependent overlap volume of depletion layers, U 4π 3 r 1 r 3 V ðÞ¼r ðÞa þ δ 3 1− þ ; ov 3 4 a þ δ 16 a þ δ is a function of the size of the polymers in solution [13]. The mini- mum value of the potential appears at r =2a,whereW(r =2a)/kT = (1 + 3a/2δ)c/c*. Hence the resulting attractive interaction can be tuned by polymer size and concentration. In the last few decades research on depletion x forces focused on equilibrium aspects of colloid–polymer mixtures: x=0 x=L the depletion interaction, phase behaviour, and scattering properties were primary focus areas [3]. A key quantity that influences colligative properties such as osmotic pressure, phase stability, diffusion and sedi- Fig. 1. Illustration of the convective depletion effect on the polymer segment concentra- tion profile between two nonadsorbing parallel walls that are permeable for solvent. mentation is the second osmotic virial coefficient B ,defined as 2 The solvent flow goes from left to right. For small flow rates of solvent through the walls Z the polymer segment concentration attains the (symmetric) equilibrium profiles (dashed ∞ ðÞà fl fi à ¼ − − Wr Ã2 Ã; ð Þ curve). For higher ow rates the polymer concentration pro les get distorted and become B2 12 1 exp r dr 2 asymmetric (solid curve). 0 kT ⁎ where r*=r/2a and B2 = B2/vc. Next we review polymer-depletion induced dynamics in colloid– Flow around a sphere mediated by the depletion effect is considered polymer mixtures and challenges encountered in systematic studies. next for it is important for estimating transport properties such as diffu- The discussion starts in Section 2 with a relatively simple case of unidi- sion [21] or sedimentation [22] of colloidal particles and proteins rectional flow of a polymer solution next to a planar nonadsorbing wall. through a solution containing macromolecules. This is related to the Then the subject is shifted towards the effect of a depletion layer on the long-time or zero-frequency limit in microrheology [23], and diffusing friction experienced by a single sphere in Section 3, followed by the wave spectroscopy measurements [24], for which it is essential to un- dynamics of two interacting particles in Section 4. The volume fraction derstand the flow induced by a colloid through a complex medium filled dependence of the diffusion coefficient, sedimentation and viscosity as with polymer chains. mediated by depletion effect is discussed subsequently in Sections 5, 6 and 7 and this paper ends with concluding remarks. 3. Motion of a sphere through a polymer solution 2. Polymer depletion dynamics at a wall and in a slit Brownian motion of a colloidal particle in a solvent originates When a solution containing nonadsorbing polymers is sheared next from the stochastic bombardment with solvent molecules. The ki- to a planar wall at constant shear stress, both the shear rate and viscos- netic energy of a colloidal particle gained from thermal fluctuations ity depend on the position from the wall surface. Once the viscosity pro- is dissipated due to hydrodynamic friction. The typical Brownian file is determined, the (apparent) slip velocity and slip (or Navier) time scale tB is approximately m/6πη0a, with particle mass m and length b can be derived. It has been shown [14] that the viscosity follows solvent viscosity η0.Attimescalet ≫ tB the translational frictional the segment density profile. The equilibrium segment density profile coefficient 6πη0a can be obtained by linear Stokes flow around the near a single planar wall reads [15] ρ(x) ≃ tanh2(x/δ), with the depletion spherical particle. As a colloidal sphere moves through a polymer thickness δ characterizing the length scale over which polymer chains solution it ‘senses’ a fluid with non-uniform viscosity, resulting in are depleted from the wall; ρ =0atthewall(x =0)andρ =1in an effective viscosity that the sphere experiences. This effective the bulk (x → ∞). For a dilute polymer solution at a planar wall an viscosity identifies how strongly sphere motion is retarded. Since analytical expression for the slip length was obtained [14]: the 1980s studies have been performed on dilute spheres translating – η pffiffiffiffiffiffiffiffiffiffi pffiffiffiffiffiffiffiffiffiffi through a polymer solution, see for instance refs [22,25 29],using ¼ δ p − ≃δ ½η −1 ½η : ð Þ experimental techniques such as dynamic light scattering, NMR, b η 1 cbtan cb 3 0 electrophoresis and sedimentation. The translational friction coeffi- cient is often interpreted in terms of the Stokes approximation in a This result describes the slip measured with computer simulations polymer solution 6πηpa,whereηp is the viscosity of the polymer with ideal polymers [16] quite well. An analytical expression for b for solution. The obtained effective viscosity ηeff that follows from the polymer chains with excluded volume interactions can also be obtained measured diffusion coefficient D0′ = kT/6πηeffa lies, however, in [17]. In practice, these results are relevant to predicting fluid flow with between the values for the viscosity of a pure solvent η0 and of the dissolved or dispersed polymers, micelles or colloids through pipes, in bulk polymer solution, ηp, implying a slip-like behaviour at the parti- interpreting measurements of the viscosity of a colloidal dispersion or cle surface. polymer solution using capillary rheometry [18], pore flow [19] or Fan et al. [30] derived analytical results for the effective viscosity using polymer solutions to sweep out oil out of natural porous media.

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