Particle Interactions

| Home | | Pharmaceutical Technology |

Chapter: Pharmaceutical Engineering: Powders

The attraction between particles or between particles and a containing boundary influences the flow and packing of powders.


The attraction between particles or between particles and a containing boundary influences the flow and packing of powders. If two particles are placed together, the cohesive bond is normally very much weaker than the mechanical strength of the particles themselves. This may be due to the distortion of the crystal lattice, which prevents the correct adlineation of the atoms or the adsorption of surface films. These prevent contact of the surfaces and usually but not always decrease cohesion. Low cohesion is also the result of small area of contact between the surfaces. On a molecular scale, surfaces are very rough, and the real area of contact will be very much smaller than the apparent area. Finally, the structure of the surface may differ from the interior structure of the particle. Nevertheless, the cohesion and adhesion that occur with all particles are appreciable. It is normally ascribed to nonspecific Van der Waal’s forces, although, in moist materials, a moisture layer can confer cohesiveness by the action of surface tension at the points of contact. For this reason, an increase in humidity can produce a sudden increase in cohesiveness and the complete loss of mobility in a powder that ceases to flow and pour. The acquisition of an electric charge by frictional movement between particles is another mechanism by which particles cohere together or adhere to containers.

These effects depend on both the chemical and physical forms of the powder. They normally oppose the gravitational and momentum forces acting on a particle during flow and therefore become more effective as the weight or size of the particle decreases. Cohesion and adhesion increase as the size decreases because the number of points in contact in a given area of apparent contact increases. The effects of cohesion will often predominate at sizes less than 100 μm and powders will not pass through quite large orifices, and vertical walls of a limited height appear in a free surface. The magnitude of cohesion also increases as the bulk density of the powder increases.

Cohesion also depends on the time for which contact is made. This is not fully understood but may be due to the gradual squeezing of air and adsorbed gases from between the approaching surfaces. The result, however, is that a system that flows under certain conditions may cease to flow when these con-ditions are restored after interruption. This is of great importance in the storage and intermittent delivery of powders. Fluctuating humidity can also destroy flow properties if a water-soluble component is present in the powder. The alternating processes of dissolution and crystallization can produce very strong bonds between particles, which cement the mass together.

Measurement of the Effects of Cohesion and Adhesion

The measurement of the cohesion between two particles or the adhesion of a particle to a boundary is difficult, although several methods can be used. More commonly, these effects are assessed by studying an assembly of particles in the form of a bed or a heap. Flow and other properties of the powder are then predicted from these studies (Crowder and Hickey, 2000).

The most commonly observed and measured property of a heap is the maximum angle at which a free powder surface can be inclined to the

FIGURE 5.1 Measurement of the angle of repose, α.

horizontal. This is the angle of repose, and it can be measured in a number of ways, four of which are shown in Figure 5.1. The angle depends to some extent on the method chosen and the size of the heap. Minimum angles are about 25, and powders with repose angles of less than 40 flow well. If the angle is over 50, the powder flows with difficulty or does not flow at all.

The angle, which is related to the tensile strength of a powder bed, increases as the particle shape departs from sphericity and as the bulk density increases. Above 100 μm, it is independent of particle size, but below this value, it increases sharply. The effect of humidity on cohesion and flow is reflected in the repose angle. Moist powders form an irregular heap with repose angles of up to 90.

A more fundamental measure is the tensile stress necessary to divide a powder bed. The powder may be dredged on to a split plate or, in a more refined apparatus, contained within a split cylinder and carefully consolidated. The stress is found from the force required to break the bed and the area of the divided surface. The principles of this method are shown in Figure 5.2A, and stresses of up to 100 N/m2 are necessary to divide a bed of fine powders. Values increase as the bulk density increases. Changes in cohesiveness with time and the severe changes in the flow properties of some powders that occur when the relative humidity exceeds 80% can be assessed with this apparatus.

Apparatus for shearing a bed of powder is shown diagrammatically in Figure 5.2B. The shear stress at failure is measured while the bed is constrained under a normal stress. The latter can be varied. The relation between these stresses, a subject fully explored in the science of soil mechanics, is used in the design of bins and hoppers for the storage and delivery of powders.

The adhesion of particles to surfaces can be studied in a number of ways. Measurement of the size of the particles retained on an upturned plate is a useful qualitative test. A common method measures the angle of inclination at which a powder bed slides on a surface, the bed itself remaining coherent.

FIGURE 5.2 Measuring the (A) tensile and (B) shear strength of a powder bed.

Contact Us, Privacy Policy, Terms and Compliant, DMCA Policy and Compliant

TH 2019 - 2024; Developed by Therithal info.