Flow Flashcards
(41 cards)
Causes of poor powder flow
1) Surface forces
- Strong attractive forces (cohesion / adhesion) –> poorer flow
- Cohesion: Between same substance
- Adhesion: Between different substances
2) Inter-particle friction
- Friction due to certain amount if rubbing/cascading when flowing
- Increased friction –> poorer flow
3) Inter-locking of particles
- Interlocking of particles –> prevent movement –> poorer flow
Types of surface forces
1) Non-specific van der Waals
2) Moisture (liquid film)
- Can form stronger bond (e.g. hydrogen bonds)
3) Electrostatic forces
4) Crystalline bridges
- May occur due to temperature change
- E.g. Condensation at lower temperatures –> may cause some dissolution –> temperature increase –> condensation dries –> solute can solidify & form solid bridges
- E.g. Melting
Factors affecting strength of surface forces
1) Particle size
- Smaller particles –> able to come closer together –> stronger forces
- Smaller particles –> greater surface area available to form surface forces
2) Contact sites (smooth VS rough)
3) Time of contact
- Certain amount of adsorbed air around particles (normal phenomenon) –> helps to separate particles to certain extent
- Longer time of contact –> air might be squeezed out –> particles able to come closer together –> stronger attractive forces
Factors affecting inter-particle friction
1) Surface of particles
- Rough surface –> more friction (VS smooth surface)
2) Size of particles
- Smaller particles –> larger surface area –> increase friction
Factors affecting inter-locking of particles
1) Size of particles
- Larger particles more likely to be interlocked
2) Size distribution
- Larger size distribution –> better packing / density –> can lock particles together
3) Shape of particles
- Irregular particles –> able to interlock
- VS Round particles –> better flow
Problems arising due to poor powder flow
1) Arching
2) Ratholing
Arching
- What is arching
- How it occurs
- How to prevent
What is arching:
Arch shaped obstruction formed above funnel –> obstruct flow
Especially with coarser powders
How it occurs:
1) Mechanical inter-locking of large particles to form an arch
2) Particles bind together to form cohesive arch
How to prevent:
1) Outlet should be > 10x D90 (from size distribution)
- Since potential problems of arching will be significant when aperture size < 6-10x max particle size
Ratholing
- What is ratholing
- How to prevent
What is ratholing:
Discharge only takes place via central flow channel located above outlet
Powder along sides of outlet will stagnate / may cake/agglomerate –> no flow
How to prevent
1) Outlet should be more angular
Glidant - Function
1) Improve flowability
Glidant - Mechanisms of actions
1) Ball bearing effect
- Correct surface irregularity –> makes particle rounder
- Rolling action –> rolling effect of glidant (small round particles)
2) Decrease inter-particle friction
- Coats surface of particles –> physical separation of particles
3) Decrease surface charge / forces
- Coat particle surface –> separate particles –> decrease inter-particle attractive forces
Glidants - Concentrations used
Used at certain concentration range for optimal activity
Excess glidant is detrimental –> glidant itself may be cohesive
Glidants - Examples
1) Talc (1 - 5%)
2) Corn starch (5 - 10%)
3) Colloidal silica (0.5 - 3%)
Flow test methods
1) Angle of repose
2) Orifice flow
3) Tapping studies
Automated methods:
1) Powder rheometer
2) Revolution powder tester
3) Shear cell
Angle of repose
Angle of inclination of a heap of powder that is built by dropping powder through a funnel onto a horizontal base
Angle of fall
Angle of repose after application of a certain shock
Angle of difference
Difference between angle of repose & angle of fall
Overcomes variation in angle of repose due to poor flow
Angle of spatula
Angle of inclination made by powder heap formed on spatula
Methods to measure angle of repose
1) Fixed funnel & free standing cone
2) Fixed bed cone
- Fixed base diameter
3) Fixed height
- Funnel fixed at pre-determined height above base
- Correction of heap height needed for apex in funnel stem
Fixed funnel & free standing cone - Limitations
1) Base diameter might not be accurate / may vary
- Can overcome by doing more heaps and getting average diameter
2) A lot of measurements to make (height, base diameter)
3) May have measurement difficulties
Fixed bed cone - Advantages
1) Less measurements needed (only need to measure height)
Fixed height - Advantages
1) Less powder needed for measurements
- As little as < 10g, if height fixed is very small
Equations to measure angle of repose
tan (angle of repose) = Height / Radius
Fixed height: h / d = (H + h) / D - h = Height of apex in funnel - H = Fixed height - d = Diameter of funnel opening - D = Base diameter tan (angle of repose) = (H+h) / Radius
Limitations in measuring angle of repose
1) High variability & high angle of repose with poor flow
2) Even with good flow, difficult to measure apex of cone
- Tend to get rounded top
- Overcome by measuring angle of repose directly with angle meter (don’t measure height)
Angle of repose & flowability
Lower angle of repose –> better flowability
Note: Angle of repose is mainly for comparative studies; Whether angle of repose is considered good/poor flow is related to use of powder