# Suspension polymerization

IUPAC definition
Polymerization in which polymer is formed in monomer, or monomer-solvent droplets
in a continuous phase that is a nonsolvent for both the monomer and the formed polymer.

Note 1: In suspension polymerization, the initiator is located mainly in the monomer phase.

Note 2: Monomer or monomer-solvent droplets in suspension polymerization have
diameters usually exceeding 10 μm.[1]
Light microscopic picture of a PMMA-copolymer, fabricated by suspension polymerization
SEM-Picture of PMMA-particles, that started to coalesce during suspension polymerization, close to a single bead
SEM-picture of a Pac-Man shaped PMMA-copolymer particle, fabricated by suspension polymerization

Suspension polymerization is a heterogeneous radical polymerization process that uses mechanical agitation to mix a monomer or mixture of monomers in a liquid phase, such as water, while the monomers polymerize, forming spheres of polymer.

This process is used in the production of many commercial resins, including polyvinyl chloride (PVC), a widely used plastic, styrene resins including polystyrene, expanded polystyrene, and high-impact polystyrene, as well as poly(styrene-acrylonitrile) and poly(methyl methacrylate).[2]

## Particle properties

Suspension polymerization is divided into two main types, depending on the morphology of the particles that result. In bead polymerization, the polymer is soluble in its monomer and the result is a smooth, translucent bead. In powder polymerization, the polymer is not soluble in its monomer and the resultant bead will be porous and irregular.[3] The morphology of the polymer can be changed by adding a monomer diluent, an inert liquid that is insoluble with the liquid matrix. The diluent changes the solubility of the polymer in the monomer and gives a measure of control over the porosity of the resulting polymer.[4]

The polymer beads that result can range in size from 100 nm to 5 mm. The size is controlled by the stirring speed, the volume fraction of monomer, the concentration and identity of the stabilizers used, and the viscosities of the different components. The following equation derived empirically summarizes some of these interactions:

${\displaystyle {\bar {d}}=k{D_{v}\cdot R\cdot \nu _{m}\cdot \epsilon \over D_{s}\cdot N\cdot \nu _{l}\cdot C_{s}}}$

d is the average particle size, k includes parameters related to the reaction vessel design, Dv is the reaction vessel diameter, Ds is the diameter of the stirrer, R is the volume ratio of the monomer to the liquid matrix, N is the stirring speed, νm and νl are the viscosity of the monomer phase and liquid matrix respectively, ε is the interfacial tension of the two phases, and Cs is the concentration of stabilizer. The most common way to control the particle size is to change the stirring speed.[4]