Effect of energy density, pH and temperature on de-aggregation in nano-particles/water suspensions in high shear mixer

Abstract The effect of energy input, pH and temperature on de-aggregation of hydrophilic silicon dioxide powder (particle size 12 nm) in a high shear mixer was investigated. It has been found that de-aggregation is a two step process. Initially, at low energy input very large aggregates (3–1000 μm) are gradually broken into smaller secondary aggregates (2–100 μm) of a single modal size distributions. As the energy input increases primary aggregates (0.03–1 μm) are eroded from the secondary aggregates leading to bimodal size distributions with the first mode between 0.03 μm and 1 μm corresponding to the primary aggregates and the second mode between 2 μm and 100 μm corresponding to the secondary aggregates. At a sufficiently high energy density all secondary aggregates are broken into primary aggregates however, even at the highest energy density employed the primary aggregates could not be broken into single nano-particles. The temperature and the pH affect de-aggregation kinetics but do not alter de-aggregation pattern. Increasing pH at low temperature speeds up de-aggregation, whilst increasing pH at high temperature slows down de-aggregation process.

[1]  E. L. Paul,et al.  Handbook of Industrial Mixing: Science and Practice , 2003 .

[2]  Ica Manas-Zloczower,et al.  Observation of carbon black agglomerate dispersion in simple shear flows , 1990 .

[3]  A. Pacek,et al.  A Process for the Manufacture of Chemically Produced Toner (CPT). I. Evolution of Structure and Rheology , 2005 .

[4]  I. Manas‐Zloczower,et al.  Influence of Particle Morphology and Flow Conditions on the Dispersion Behavior of Fumed Silica in Silicone Polymers , 2004 .

[5]  S. Pratsinis,et al.  Energy—size reduction laws for ultrasonic fragmentation , 1994 .

[6]  A. Pacek,et al.  Video technique for measuring dynamics of liquid‐liquid dispersion during phase inversion , 1994 .

[7]  R. Iler The Chemistry of Silica: Solubility, Polymerization, Colloid and Surface Properties and Biochemistry of Silica , 1979 .

[8]  Kevin Kendall,et al.  Adhesion and aggregation of fine particles , 2001 .

[9]  Richard M. Pashley,et al.  Hydration forces between mica surfaces in electrolyte solutions , 1982 .

[10]  Eric Forssberg,et al.  Prediction of product size distributions for a stirred ball mill , 1995 .

[11]  R. Yoon,et al.  Application of Extended DLVO Theory: II. Stability of Silica Suspensions , 1993 .

[12]  Krister Holmberg,et al.  Handbook of applied surface and colloid chemistry , 2002 .

[13]  Roe-Hoan Yoon,et al.  Application of Extended DLVO Theory , 1993 .

[14]  J. Israelachvili Intermolecular and surface forces , 1985 .

[15]  Lee R. White,et al.  The calculation of hamaker constants from liftshitz theory with applications to wetting phenomena , 1980 .

[16]  Wolfgang Peukert,et al.  Prediction of aggregation kinetics based on surface properties of nanoparticles , 2005 .

[17]  R. Horn,et al.  Double-Layer and Hydration Forces Measured between Silica Sheets Subjected to Various Surface Treatments , 1993 .

[18]  H. Schubert,et al.  Developments in the continuous mechanical production of oil-in-water macro-emulsions , 1995 .

[19]  Jörg Schwedes,et al.  Mechanical production and stabilization of submicron particles in stirred media mills , 2003 .

[20]  F. Stenger,et al.  Control of aggregation in production and handling of nanoparticles , 2005 .