What is Diffusivity?
Diffusivity is the average speed of a solute moving through a solvent. Here, we are focused primarily on solute self-diffusion within a hydrogel. In that case, the solute is moving via Brownian motion, so the only forces acting on it are the bouncing around of nearby molecules. Convection and chemical gradients are minimized by the hydrogel keeping water molecules relatively stable and incubating the hydrogel in a large reservoir of the solute-containing solution until equilibrium, resulting in a homogeneous distribution of the solute throughout the interior of the hydrogel.
What is the Relevant Property?
The Diffusion Coefficient is the most commonly used property for self-diffusion of a solute within a hydrogel. With common units of μm2/s for a solute in a liquid, the diffusion coefficient is an intermediate term relating the flux of a solute (J) to its concentration change (dc) over distance (dx) (Fick’s law equation below).
\begin{align*} J = -D\frac{dc}{dx} \end{align*}In a hydrogel, two diffusion coefficients are relevant: the diffusion coefficient of the solute within the gel (D) and the diffusion coefficient of the solute in water (D0). Since the diffusion coefficient of solutes in water can generally be calculated using the Stokes-Einstein equation (below) current experimental and theoretical study is focused on understanding how much the hydrogel can affect solute diffusion based on the ratio of D/D0.
\begin{align*} D_{0} = \frac{k_{b} T}{6\pi \eta r_{s}} \end{align*}Alternative Parameters:
Because the diffusion coefficient is well established through Fick’s Law and the highly effective Stokes-Einstein equation, alternative parameters are not commonly used. However, care must be taken to evaluate whether the diffusion coefficient is a self-diffusion coefficient, characterized by a lack of convection and chemical gradients, or another kind of diffusion coefficient, such as the steady state diffusion coefficient of a gradient-motivated diffusion.
How is it Measured?
Measuring self-diffusion coefficients in a hydrogel requires the solute concentration within the hydrogel to be homogeneous and in steady state equilibrium, so traditional measurement methods for gradient diffusion, such as loading and release or use as a membrane in a diffusion cell are not an option. Instead, advanced fluorescence microscopy techniques or diffusion-sensitive NMR must be used.
Fluorescence Recovery After Photobleaching (FRAP)
Fluorescence recovery after photobleaching (FRAP) uses a highly powered confocal fluorescence microscope to permanently bleach a region of fluorophores within the hydrogel then record at a lower power as fluorescing particles diffuse back into that region and non-fluorescing particles move outward. Since the photobleaching effect does not otherwise change the solutes, this method is still effectively self-diffusion. Fluorescein is a strong candidate for FRAP in hydrogels since it is water soluble, can photobleach, and can be conjugated to many molecules as the modified fluorescein isothiocyanate (FITC). The analysis of FRAP data involves tracking the intensity distribution in and around the photobleached spot over time. Powerful mathematical and algorithmic tools have been developed to analyze FRAP data, and we have recently published a modified MATLAB program that is optimized for high throughput analysis of FRAP data for solute diffusion within hydrogels (Richbourg & Peppas, 2021; see also the Tools Page).
Fluorescence Correlation Spectroscopy (FCS)
Fluorescence Correlation Spectroscopy (FCS) focuses a microscope on a very small volume, records the period of each event in which a fluorescent molecule is moving within that volume, and correlates that data to a diffusion coefficient. Unlike FRAP, FCS requires a precisely calibrated instrument and consistent solute behavior: misunderstanding the illuminated volume distorts calculation of the diffusion coefficient, and solute variability yields an anomalous correlation curve that is more difficult to interpret. While FCS has potential for insight regarding diffusion in hydrogels, its applications are more limited than the broadly applicable and robust FRAP alternative. An example of FCS used to study solute diffusion in hydrogels: [Zustiak et al., 2010].
Diffusion-Ordered Spectroscopy Nuclear Magnetic Resonance (DOSY NMR)
Diffusion-Ordered Spectroscopy Nuclear Magnetic Resonance (DOSY NMR) uses proton NMR to identify solutes and the induced dipole moment associated with NMR to evaluate solute self-diffusion. Like FCS, DOSY NMR can be greatly affected by solute heterogeneity. DOSY NMR also requires that the hydrogel-solute combo be gelled within an NMR tube and with deuterated water, which somewhat limits its use for studying solute diffusion within hydrogels.
Related Properties
Several properties relate to solute diffusion, though the relationships are not always clear. Some of the properties are intermediate values within the swollen polymer network model, such as the solute hydrodynamic radius and mesh radius. Other properties, such as the partition coefficient and the kinetics of solute loading and release into hydrogels are not addressed but should be addressed in future developments. Swollen polymer volume fraction has a strong influence on solute diffusion in hydrogels, but it is not included here since it is addressed on the swelling page.
Partition Coefficient (K)
Partition Coefficients (K) describe the partitioning of solutes between a hydrogel and the surrounding bulk solution at equilibrium. Partition coefficients are always context-specific, as they can be affected by the concentration in the bulk solution, the geometry and size of the hydrogel, and other factors, but under consistent conditions they can provide some insight about the interactions between the solute and the hydrogel. Typically, a partition coefficient greater than one indicates that the solute has a chemical affinity for the polymer used in the hydrogel. Partition coefficients less than one could be affected by chemical repulsion or the structure of the hydrogel limiting the movement of solute into the hydrogel. Large solutes can be systematically excluded by highly crosslinked hydrogels, which will greatly lower their partition coefficients.
Partition coefficients are most simply defined for hydrogels as the concentration within the hydrogel divided by the concentration outside the hydrogel (equation below).
\begin{align*} K = \frac{C_{gel}}{C_{sol}} \end{align*}A common method for calculating partition coefficients within a hydrogel is to measure the concentration within the solution before introducing the hydrogel and measure it after equilibrium to calculate the reduction in concentration and assume the associated mass of solute was transferred into the gel. The equation below makes that calculation given the volume of the solution (Vsol) and the volume of the gel (Vgel).
\begin{align*} K = \frac{V_{sol} \left(C_{0} – C_{eq}\right)}{V_{gel} C_{eq}} \end{align*}However, this approach assumes that there is no fouling, or accumulation of the solute at the surface of the hydrogel. Our experiments have shown that there is usually solute fouling at the surface of a hydrogel, so we instead use a confocal microscope to measure the average intensity within the hydrogel and correlate that to a concentration based on a standard curve.
Additionally, if you assume all of the solute stays within the aqueous phase of the hydrogel, it is reasonable to calculate an “Enhancement factor” [Kotsmar et al., 2012] from the partition coefficient, which estimates the solute concentration within the aqueous phase of the hydrogel by deducting the swollen polymer volume fraction (equation below).
\begin{align*} E = \frac{K}{1-\phi_{s}} \end{align*}Currently, the relationship between a solute’s self-diffusion coefficient within a hydrogel and the partition coefficients is not well-defined, but it is likely important since diffusion coefficients are sensitive to concentration.
Solute Hydrodynamic Radius (rs)
The Solute Hydrodynamic Radius (rs) is the estimated radius of the solute within an aqueous solution assuming it is a hard sphere. Hydrodynamic radii are typically calculated from a solute’s self diffusion coefficient in aqueous solution via the Stokes-Einstein equation.
\begin{align*} D_{0} = \frac{k_{b} T}{6\pi \eta r_{s}} \end{align*}Hydrodynamic radius is often treated as the defining parameter for a solute’s size, but it does not account for flexibility or non-sphericality, which play a more significant role for diffusion within a hydrogel than diffusion within free solution.
Mesh Size (ξ) and Mesh Radius (rm)
Mesh Size (ξ) is the hydrogel structural parameter most closely associated with solute diffusion in a hydrogel, although the swollen polymer volume fraction is also considered a strong influence. Definitions of mesh size have differed between groups and over time, but the most conceptually consistent definition of mesh size is the average distance between h=network junctions that are connected by a single chain. Since mesh size is a distance, it does not correspond perfectly to degree of polymerization between junctions (Nj) or the frequently discussed molecular weight between crosslinks (Mc). Two chains with the same degree of polymerization between junctions can have different mesh sizes if they are extended to different lengths. Because mesh sizes are typically on the order of nanometers in a synthetic hydrogel and must be measured in a hydrated state to be accurate, they are most often estimated based on more readily measured properties such as the swollen polymer volume fraction. As shown on the Mesh Transport Theory page, we use a modified Canal-Peppas equation to calculate mesh size [Richbourg & Peppas, 2020].
Mesh Radius (rm) is a concept we introduced recently to address the effect of variable junction functionality on solute transport within hydrogels [Richbourg, Ravikumar, and Peppas, 2021]. A hydrogel’s mesh radius is the maximum radius of a solute that can pass through the hydrogel network’s portals. It is important to dinstinguish between mesh size and mesh radius because mesh radius has a more direct influence on solute transport within a hydrogel, and the same mesh size can result in different mesh radii based on the junction functionality and geometry of the hydrogel. For example, a perfect hydrogel with a junction functionality of 6 would have cubical cells with square portals, so the mesh radius would be half of the mesh size. But for a hydrogel with a junction functionality of 4, or tetrahedral junctions, the mesh radius would be a larger fraction of the mesh size due to the more open geometry. Mesh radius calculations are also provided on the Mesh Transport Theory page.
Solute Loading and Release Kinetics (D?)
Solute loading and release kinetics differ from self-diffusion in that the solute is diffusing into a solute-free hydrogel or from the hydrogel into an empty reservoir. Both cases are driven by chemical gradients and are therefore a little more complicated than self-diffusion conditions. One major factor that is relevant in loading and release but not in self-diffusion is the boundary between the hydrogel and the surrounding solution, that can create unique interactions such as solute accumulation at the surface, known as “fouling.” Fouling can slow transport into the hydrogel and cause initial burst releases when unloading from the hydrogel. It is currently unclear whether solute loading and release can be described using the same Mesh Transport Theory equations, but the consistent use of diffusion coefficients to describe loading and release behavior and self-diffusion suggests there could be comparable relationships.
Our Results on Structural Design of Solute Diffusivities in Hydrogels
Our published work in Macromolecules for PVA hydrogel and our follow-up studies with multi-arm PEG hydrogels in Journal of Materials Chemistry B summarizes our results so far on structural design of solute diffusivities in hydrogels. Like with our swelling results, we created PVA hydrogels with three initial polymer volume fractions (φ0) and six degrees of polymerization between junctions (Nj), yielding 18 PVA hydrogel formulations. We then incubated each formulation with each of seven solutes: fluorescein, three sizes of FITC-dextran, a globular, highly branched polysaccharide (4, 20, 70 kDa), and three sizes of FITC-PEG, a linear synthetic polymer (5, 20, 40 kDa). FRAP experiments on each combination yielded diffusion coefficients that we compared to understand how solute size and type and hydrogel structure affect solute self-diffusion in hydrogels.
With the multi-arm PEG hydrogels, we varied all four structural parameters simultaneously, measured diffusion and partitioning in each hydrogel formulation for fluorescein, 4 kDa FITC-dextran, and 20 kDa FITC-dextran, and tested our mesh radius hypothesis.
Our major results from the PVA hydrogel study are summarized below:
In free solution, FRAP-measured solute diffusivities closely matched Stokes-Einstein model predictions.
Model predictions wildly underestimated the influence of solute size on diffusivities within hydrogels.
For fluorescein and FITC-dextrans, increasing solute size generally reduced diffusivity, but opposite trend was observed for FITC-PEGs.
Increasing hydrogel mesh radius corresponded to increasing diffusivities for all solutes, suggesting hydrogel structural design can control solute transport within hydrogels.
Our major results from the multi-arm PEG hydrogel studies are listed below: