Potato starch has been acetylated in a counter rotating twin strew ext
ruder using vinylacetate and sodium hydroxide. The desired starch acet
ylation reaction is accompanied by an undesired parallel base catalyse
d hydrolysis reaction of vinylacetate and a consecutive hydrolysis rea
ction oi. the acetylated starch. Also deacetylation may occur. During
the extrusion process sodium hydroxide, vinylacetate, granular potato
starch and water were supplied to the extruder. Conversions up to 100
% could be achieved. The degree of substitution could be varied from 0
.05 to 0.2. Selectivities from vinylacetate towards starch of up to 80
% could be achieved. From reaction kinetics and experiments it could b
e concluded that the deacetylation reaction could be neglected. The de
gree of gelatinisation appeared to be a major key parameter. Increasin
g the gelatinisation in an early stage of the extrusion process, at hi
gh starch concentrations and temperatures, increases the selectivity a
nd degree of substitution. The gelatinisation degree can be increased
by applying high shear and temperatures to the starch granule and by u
sing screws with modified geometries.