A new segmented flow tubular reactor for the continuous production of powde
rs was used to synthesize calcium carbonate by precipitation. This new reac
tor uses a nonmiscible phase (air in most cases) to create individual micro
volumes of the reacting mixture or suspension ensuring that a plug-flow reg
ime is maintained. In a microvolume, poor micromixing can be avoided and th
e homogeneity in reaction conditions is increased better than in larger vol
umes, leading to a better control of powder characteristics. Calcium carbon
ate with controlled characteristics could be precipitated continuously usin
g this new segmented flow tubular reactor. Pure calcite could be obtained i
n the tubular reactor by segmenting a Ca2+ solution with a reactive CO2/NH3
gas mixture. This synthesis process is very promising for industrial produ
ction since the scale-up should easily be achieved by multiplying the numbe
r of tubes working in parallel.