LED-based particle image velocimetry (PIV) images the velocity field inside a moving powder bed during blending, adding spatial resolution that static angle of repose, Hausner ratio, and shear cell tests cannot provide. Here is what that resolution can and cannot support for a process decision.
Co-processing engineers particle morphology, density, and surface structure into a single composite excipient particle. Flow function and compactibility testing show what that buys formulators on continuous direct compression lines, and where it does not.
The power or torque trace in high-shear wet granulation rises and plateaus as granules consolidate, but the signal is a supporting process indicator, not a direct particle size measurement, and its interpretation is bounded by batch size, impeller geometry, and formulation.
The same screw feeder at the same speed can deliver consistently on one powder and drift by several percent on another. The difference lies in compressibility, wall friction, and cohesion, and in how bulk density shifts as the hopper empties.
Paint QC can approve a batch that still behaves [...]
Powder segregation diagnosis starts by locating where the [...]
The powder percolation threshold is the point where [...]
Powder behavior control starts with fifteen core factors. [...]
Changeovers can quietly waste hours and tons of [...]
Dry electrode battery manufacturing demands tighter powder control. [...]
