Vented extruder devolatilization (DV) of PS melt containing 6, 000 ppm
styrene was studied by scanning electron microscopy (SEM) and video p
hotography. Vacuum DV of a polymer is accompanied by foaming, which st
arts instantaneously upon supersaturation of the stretched melt and is
enhanced at higher speeds of the vented extruder screw. As the volati
les are removed from the melt, foaming gradually ceases, starting with
the pushing flight of the screw. The experimental installation design
allowed us to quench the polymer melt in the DV zone at various stage
s of the process. Samples taken from four areas of the channel width w
ere investigated by SEM. Bubble nucleation in the melt appears to take
place mainly in the border area adjoining the gas phase. In the shear
field caused by screw rotation, large bubbles become noticeably elong
ated. Their surface, as well as the free surface of the melt, is cover
ed with blisters, 1-100 mum in size. Microblisters are often concentra
ted in areas subjected to stretching. Calculations of cooling due to v
olatile evaporation and of heating due to viscous dissipation near a g
rowing bubble shows that the process of foam-enhanced DV of a PS/styre
ne system can be regarded isothermal if the initial volatile concentra
tion does not exceed approximately 1%.