Question

In: Other

Q. Spherical glass particles (12 mm diameter and 2500 kg/m 3 density) and spherical metal particles...

Q. Spherical glass particles (12 mm diameter and 2500 kg/m 3 density) and spherical metal particles (1.5 mm diameter and 7500 kg/m3) are falling in water (density= 1000 kg/m3) .

(1) Calculate the terminal falling velocities of glass and metal particles in water for a constant friction factor of 0.22.

(2) At what water velocity will fluidized beds of glass particles and metal particles have the same bed densities?

The relation between fluidization velocity (uc), terminal velocity (ut) and bed voidage (e) for a spherical particle is given by the equation (uclut) = e2·3

Solutions

Expert Solution

Step 1

Given that:

Spherical glass particle has a diameter(D1) =12mm and density() = 2500 kg/m3,

Spherical metal particle has diameter(D2) = 1.5mm and density() = 7500 kg/m3

Falling water density() = 1000 kg/m3

Step 2

Equation for the sphere balance,

where,

That is equal to the

For metal particles,

Put all the values in the above equation to get the velocity of the terminal falling velocity of the metal particle,

on solving the above equation we get velocity,

u0 = 0.5356 m/s

For the glass particle,

u0 = 0.7278 m/s

Step 3

We have an equation for the fluidized bed,

The density of the suspension =

uc is the fluidized velocity, ut is the terminal velocity and e is the bed voidage.

For glass particles:

(uc/0.7278) = e12.30

For the metal particles:

(uc/0.536) = e22.30

By dividing equation metal particles to the glass particles we get,

On cancellation of uc

0.7278/0.536 = (e2/e1)2.30

(e2/e1) = (0.7278/0.536)1/2.30 = 1.142

e2 = 1.142e1

b) For equal bed densities:

Put all the values in the above equation to get the value of bed voidage(e)

e1 * 1000kg/m3 + (1 - e1) * 2500kg/m3 = 1.142e1 * 1000kg/m3 + (1 - 1.142e1) * 7500kg/m3

1000e1 + 2500kg/m3 - 2500(kg/m3)e1 = 1142(kg/m3)e1 + 7500kg/m3 - 8565(kg/m3)e1

Taking e1 common on both side we get,

e1(1000kg/m3 -2500kg/m3 -1142kg/m3 +8565kg/m3 ) = 7500kg/m3 -2500kg/m3

e1(5926kg/m3) = 5000kg/m3

dividing both side by 5926 we get,

e1 = 0.844

and e2 = 1.142* e1 = 1.142*0.844 => 0.96355

For glass particles

(uc/0.7278) = e12.30

uc = (0.844)2.30 * 0.7278 => 0.492 m/s

By putting the value of e1 we have uc

uc = 0.492 m/s

For the metal particles:

(uc/0.536) = e22.30

uc = (0.96355)2.30 * 0.536 => 0.492 m/s

By putting the value of e2 we have uc

uc = 0.492 m/s

At 0.492 m/s water velocity would be same bed densities.


Related Solutions

130 kg of uniform spherical particles with a diameter of 60 mm and particle density 1500...
130 kg of uniform spherical particles with a diameter of 60 mm and particle density 1500 kg/m3 are fludised by water (density 1000 kg/m3, viscosity 0.001 Pa s) in a circular bed of cross-sectional area 0.2 m2. The single particle terminal velocity of the particles is 0.98 mm/s and the voidage at incipient fludisation is known to be 0.47. Determine: a. The minimum fludised velocity             b. height when the liquid flow rate is 2x10-5 m3/s.  
130 kg of uniform spherical particles with a diameter of 60 mm and particle density 1500...
130 kg of uniform spherical particles with a diameter of 60 mm and particle density 1500 kg/m3 are fludised by water (density 1000 kg/m3, viscosity 0.001 Pa s) in a circular bed of cross-sectional area 0.2 m2. The single particle terminal velocity of the particles is 0.98 mm/s and the voidage at incipient fludisation is known to be 0.47. Determine: The minimum fludised velocity and the bed height at incipient fludisation.                                The mean fludised bed voidage and height when...
A packed bed of uniform spherical particles of diameter, d= 2.5 mm, density ρs= 4000 kg/m3...
A packed bed of uniform spherical particles of diameter, d= 2.5 mm, density ρs= 4000 kg/m3 , and voidage e= 0.45 is fluidised by means of a liquid of viscosity μ= 1 mN s/m2 and density ρ= 900 kg/m3 . (a) Starting from Carman’s and Ergun’s equations reported in the attached equations sheet, derive the corresponding expressions for the minimum fluidising velocity, umf, for both equations and explain their meaning.
Approximately spherical particles of diameter 150? and density 2650 kg/m3 settle through a liquid of density...
Approximately spherical particles of diameter 150? and density 2650 kg/m3 settle through a liquid of density 1097 kg/m3 and dynamic viscosity 3.8 mPa s. The volume fraction of particles is 30% in a container of internal diameter 2 cm Calculate: a)The absolute settling velocity that is apparent to the stationary observer in the lab frame. b)The slip velocity (Us) between solid and liquid phases. c) The superficial velocity of the particles in the lab frame.
You have a glass ball with a radius of 2.00 mm and a density of 2500...
You have a glass ball with a radius of 2.00 mm and a density of 2500 kg/m3. You hold the ball so it is fully submerged, just below the surface, in a tall cylinder full of glycerin, and then release the ball from rest. Take the viscosity of glycerin to be 1.5 Pa s and the density of glycerin to be 1250 kg/m3. Use g = 10 N/kg = 10 m/s2. Also, note that the drag force on a ball...
Solid particles of density 2500 kgm-3 were packed into a fluidized bed reactor of 2 m...
Solid particles of density 2500 kgm-3 were packed into a fluidized bed reactor of 2 m in height and 0.04 m2 in cross-sectional area. The mass and height of the packed bed are 45 kg and 1 m, respectively. The surface-volume mean diameter of the particles is 1 mm. (a) Determine the porosity of the packed bed. (b) Determine the pressure drop across the bed when a liquid of density 800 kgm-3 and viscosity of 0.002 Pa s flows through...
A bubble is sphere with 10 mm radius and a density of 1.0 kg/m^3. This goes...
A bubble is sphere with 10 mm radius and a density of 1.0 kg/m^3. This goes up in a glass of water which has Pwater=0.95 g/cm^3. It starts at the bottom of a glass which is 10 cm tall. Cd=0.8 Hypothesize how long it would take the bubble to rise to the top of the glass. Draw a complete force diagram of the bubble, including weight, buoyancy and drag forces. Make sure your coordinate axis points in the direction of...
Solid particles (diameter 1.5 x 10-4 m, average density = 2800 kg/m3) are settling in water...
Solid particles (diameter 1.5 x 10-4 m, average density = 2800 kg/m3) are settling in water at 30 °C. The properties of water at this temperature are viscosity (µ) = 8 x 10-4 kg/m.s and density (p) = 996 kg/m3 a) What is the terminal velocity for the particles? b) What would be the velocity of the system in a separator with an acceleration of 390 m/s2?
A 1-mm diameter sphere (density=7900 kg/m3) is dropped into a tank of oil (density=900 kg/m3). The...
A 1-mm diameter sphere (density=7900 kg/m3) is dropped into a tank of oil (density=900 kg/m3). The sphere develops a terminal speed of 0.25 cm/s, what is the oil's viscosity? You may assume a small Reynolds number. Show your work.
A 60 kg Drum of diameter 40 cm containing waste material of density 1100 kg/m^3 is...
A 60 kg Drum of diameter 40 cm containing waste material of density 1100 kg/m^3 is being lifted by a steel cable of diameter 30 mm. When the drum is hoisted 10m the natural frequency is measured to be 40 Hz. Determine the volume of the waste in the drum.
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT