Motion of particles trough fluids part 2

1. Motion of particles trough fluidspart 2 By: Mdm. Noor Amirah Abdul Halim

2. Particle settling Free settling • When a particle is at sufficient distance from the wall of the container and from other particle, so that its fall is not affected by them, the process is called free settling. • Terminal velocity is also known as free settling velocity. Hindered settling • When the particles are crowded, they settle at a lower rate and the process is called hindered settling. • The particles will interfere with the motion of individual particles • The velocity gradient of each particle are affected by the close presence of other particles.

3. Hindered settling • The velocity for hindered setting can be computed by this equation: • Where, ε is volume fraction of the slurry mixture and Ψp is empirical correction factor. • Bulk density of mixture – • Empirical correction factor - Correction factor Stokes Law

4. Hindered settling The Reynolds number is then based on the velocity relative to the fluid is Where the viscosity of the mixture µm is given by;

5. Exercise • Calculate the settling velocity of glass spheres having a diameter of 1.554 x10-4 m in water at 20ºC The slurry contains 60 wt % solids. The density of the glass sphere and water is 2467kg/m3 and 998 kg/m3 respectively. • Calculate the Reynold number for this settling.

6. Fluidization • Fluidization is a process whereby a granular material is converted from a static solid-like state to a dynamic fluid-like state. • This process occurs when a fluid (liquid or gas) is passed up through the granular material. • The most common reason for fluidizing a bed is to obtain vigorous agitation of the solids in contact with the fluid, leading to an enhanced transport mechanism (diffusion, convection, and mass/energy transfer). 

7. Fluidized Bed Reactor

8. When a gas flow is introduced through the bottom of a bed of solid particles, it will move upwards through the bed via the empty spaces between the particles.  • At low gas velocities, aerodynamic drag on each particle is also low, and thus the bed remains in a fixed state. • Increasing the velocity, the aerodynamic drag forces will begin to counteract the gravitational forces, causing the bed to expand in volume as the particles move away from each other • Further increasing the velocity, it will reach a critical value at which the upward drag forces will exactly equal the downward gravitational forces, causing the particles to become suspended within the fluid. At this critical value, the bed is said to be fluidized and will exhibit fluidic behavior.

9. By further increasing gas velocity, the bulk density of the bed will continue to decrease, and its fluidization becomes more violent, until the particles no longer form a bed and are “conveyed” upwards by the gas flow. • When fluidized, a bed of solid particles will behave as a fluid, like a liquid or gas. • Objects with a lower density than the bed density will float on its surface, bobbing up and down if pushed downwards, while objects with a higher density sink to the bottom of the bed • The fluidic behavior allows the particles to be transported like a fluid, channeled through pipes, not requiring mechanical transport

10. Applications of Fluidization

11. Conditions for Fluidization

12. Based on the Figure: • If the superficial velocity, VOis gradually increased, the pressure drop will increases, but the particles do not move and the height (L) remains the same. • At a certain velocity, the pressure drop across the bed counterbalances the forces of gravity on the particles or the weight of the bed • At point A = Any further increase in velocity, causes the particles to move • At point B = Further increase in velocity, the particles become separate enough to move about in the bed and true fluidization begins.

13. From point B to point C = Once bed is fluidized, the pressure drop across the bed stays constant , but the bed heights continues to increase with increasing velocity. • From point C to B = If the velocity is gradually reduced, the pressure drop remains constant and the bed height decreases. *The pressure drop required for the liquid or the gas to flow through the column at a specific flow rate

14. Minimum Fluidization Velocity • Minimum velocity of fluidization took place at incipient (beginning) fluidization. • During this stage, the ratio of pressure drop to the vessel height (L) is given by; • Where is the minimum porosity

15. The minimum fluidization velocity can be obtained by this equation; • For roughly spherical particles, is generally between 0.4 and 0.45 (commonly taken as 0.45) which increasing slightly with decreasing particle diameter.

16. Exercise • A bed of ion exchange beads 8 ft deep is to be backwashed with water to remove dirt. The particles have a density of 1.24 g/cm3 and an average size of 1.1 mm. The beads are assumed to be spherical (Φ =1) and is taken as 0.4. What is the minimum fluidization velocity using water at 20ºC with density of 980 kg/m3?