The conventional method for the synthesis of porous crosslinked copolymer b
eads is by suspension polymerisation. Suspension polymerisation reactions a
re generally performed in a stirred tank, which generally results in a larg
e size distribution. By careful control of the polymerisation conditions, p
olymer beads can be produced using a tubular poly(tetrafluoroethylene) cont
inuous reactor. Such beads are produced with the same average pore size, bu
t with a lower degree of polydispersity than analogous systems produced in
a batch reactor (stirred tank). This is achieved by density-matching the dr
oplet and continuous phases (by the use of a brominated monomer or a poroge
nic diluent) and increasing the viscosity of the monomer phase (with the ad
dition of small amounts of polystyrene).