Presentation on theme: "Motion of particles trough fluids part 2"— Presentation transcript:
1 Motion of particles trough fluids part 2 By: Dr Akmal Hadi Bin Ma’ Radzi
2 Particle settling Free settling Hindered 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 settlingWhen 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 particlesThe velocity gradient of each particle are affected by the close presence of other particles.
3 Hindered settlingThe 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 factorStokes Law
4 Hindered settlingThe Reynolds number is then based on the velocity relative to the fluid is Where the viscosity of the mixture µm is given by;
5 ExerciseCalculate the settling velocity of glass spheres having a diameter of 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 SolutionDensity of the water = 998 kg/m3, and viscosity of water μ = x 10-3 Pa.s. To calculate the volume fraction ɛ of the liquid, The bulk density of the slurry m is Then,
7 The terminal velocity is: The Reynolds number can be calculated as follows: NRe
8 FluidizationFluidization 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).
10 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 otherFurther 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.
11 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 bedThe fluidic behavior allows the particles to be transported like a fluid, channeled through pipes, not requiring mechanical transport
14 Based on the Figure:If the superficial velocity, VO is 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 bedAt point A = Any further increase in velocity, causes the particles to moveAt point B = Further increase in velocity, the particles become separate enough to move about in the bed and true fluidization begins.
15 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
16 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
17 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.
18 If the Reynolds number is used, then, The equation becomes:
19 Exercise 2A 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?
21 Exercise 3Solid particles having a size of 0.12 mm, a shape factor Фs of 0.88, and a density of 1000 kg/m3 are to be fluidized using air at 2.0 atm abs and 25 oC. The voidage at minimum fluidizing condition is 0.42.If the cross section of the empty bed is 0.30 m2 and the bed contains 300 kg of solid, calculate the minimum height of the fluidized bed.Calculate the pressure drop at minimum fluidizing conditionsCalculate the minimum velocity of fluidization
22 For part (a), the volume of solids = 300 kg/(1000 kg/m3) = 0. 300 m3 For part (a), the volume of solids = 300 kg/(1000 kg/m3) = m3. The height of the solids would occupy in the bed if ɛ1 = 0 is L1 = 0.300m3/(0.30m2 cross section) = 1.00 m. Solving Lmf = m
23 The physical properties of air at 2. 0 atm and 25 oC are μ = 1 The physical properties of air at 2.0 atm and 25 oC are μ = x 10-5 Pa.s, = x 2 = kg/m3, and p = x 105 Pa. For the particle, Dp = m, p= 1000 kg/m3, s = 0.88 and ɛmf = For part (b), To calculate Vmf’ for part (c),