POLYMER SOLUBILITY AND SOLUBILITY PARAMETER
Solubility parameters were initially developed to guide solvent selection in the paint and coatings industry. Today, they are widely used in in many other fields to predict miscibility and solubility of polymers, chemical resistance, and permeation rates.
One of
the most important application of solubility parameters is the prediction of
polymer solubility in solvents. The closer the solubility parameters of the
solute and the solvent are, the more likely the solubility of the solute in the
given solvent.
In the case of polymers, there are several rules of thumb for selecting
suitable solvents:
a. |δs - δp| ≤ 3.6 MPa1/2
· Using Hansen solubility parameters, an approximate spherical "volume" of solubility with radius R can be drawn up for each solute. Only solvents that have Hansen solubility parameters within this volume are likely to dissolve the polymer in question:
a. [4(δd2 - δd1)2 + (δp2 - δp1)2 + (δh2 - δh1)2]1/2 ≤ R
b. The interaction radius, R, depends on the type of polymer. The R values are usually in the range of 4 to 15 MPa1/2.
It is important to note that the higher the molecular weight of a polymer, the closer the solubility parameter of the solvent and polymer need to be to dissolve the polymer in the solvent. For linear and branched polymers, a plot of solubility versus solubility parameter for a range of solvents will peak when the (Hansen / Hildebrand) solubility parameters of the solute and solvent match. In the case of a cross-linked polymer, the swell volume, i.e. the solvent uptake, will peak when the solubility parameters of the solvent match those of the polymer.
As a general rule, the solubility parameters of polymers do not change much with temperature, whereas those of low molecular weight compounds often decrease noticeably with increasing temperature. In some cases, a solvent passes through soluble conditions to once more to become a non-solvent as the temperature increases.
For regular solutions1 in which intermolecular (specific) attractions are minimal and the solution diverges only moderately from the ideal solution*, the enthalpy of mixing can be estimated from the solubility parameters as proposed by Hildebrand and Scott:2
ΔH1,2 ≈ ΔU1,2 = φ1 φ2 (δ1 – δ2)2
where ΔU1,2 is the internal energy change of mixing per unit volume and φ1 and φ2are the volume fractions of the solvent and the polymer in the mixture.