Slip casting of Si3N4 requires well-dispersed low viscosity suspension
s. Two alternative procedures have been applied: (a) premixing by attr
itor milling in isopropanol, drying followed by the final slip prepara
tion with deflocculant and water in a ball mill (batch A) and (b) susp
ending the powder in water using a deflocculant and mixing milling in
a continuous attritor-like mill (batch B). Both batches were identical
with respect to the starting powder, additives and the solid content.
Astonishingly, the rheology was found to be quite different. Batch A
had a strong tendency to Bingham behaviour whereas batch B showed a cl
ear Newtonian shear curve. The differences are attributed to a reactio
n of the alcohol used (isopropanol) in batch A with the powder surface
s forming stable surface groups. The most probable configuration is a
silyl ester Si-O-C-R, shielding the active sites against the coupling
of the deflocculants. Burn-out experiments revealed that temperatures
of 500-degrees-C are necessary to remove these surface groups. After t
his treatment the powders could be suspended giving the same shear cur
ve as batch B.