Question

In: Civil Engineering

Compute the settling velocity for the following particles: very coarse sand ( diameter = 1.5 mm...

Compute the settling velocity for the following particles: very coarse sand ( diameter = 1.5 mm ) , (diameter=1.5 mm), medium sand (0.4 mm), very fine sand (0.075 mm), and clay (0.001 mm). Estimate the time for each particle to fall 6 in. in water.

Assume: SG: coarse sand = 2.65, medium sand = 2.67, fine sand = 2.70, clay = 2.8 & water temperature = 60°F

Note:The other solution on chegg is wrong.

Solutions

Expert Solution

Salution:

Given data:

Very coarse sand diameter d1 = 1.5 mm

SG of coarse sand = G1 =2.65

Medium sand diameter d2 = 0.4 mm

SG of medium sand = G2= 2.67

Very fine sand diameter d3 =0.075 mm

SG of fine sand = G3 = 2.70

clay particals diameter d4 = 0.001 mm

SG of clay = G4 = 2.8

g = 9.81 m/sec2

Say kinematic viscosity of water =   = 1.787 x 10-6 m2 s-1

(a)

=>

Very coarse sand diameter d1 = 1.5 mm

SG of coarse sand = G1 =2.65

Partical diameter =d1 = 1.5 mm > 1 mm

Turbulent settling velocity = Vs =1.8  { g d (G-1) } = 1.8  { g d1 (G1-1) } = 1.8 { 9.81 x (1.5/1000) (2.65-1) }

Vs = 0.2805 m/sec

Velocity for very coarse sand ( diameter = 1.5 mm ) is 0.2805 m/sec.....................(Answer)

Fall = h = 6" = 0.1524 meter

6" Fall time =t = h/Vs = 0.1524 m / 0.2805 m/sec = 0.5433 second........................(Answer)

(b)

=>

Medium sand diameter d2 = 0.4 mm

SG of medium sand = G2= 2.67

Water Temparature = T =60°F = { (60°F − 32) × 5/9 } = 15.556°C

Partical diameter =d2 = 0.47 mm , 0.1 mm <d2 < 1 mm

Settling velocity = Vs =418 (G-1 ) d {(3T+70)/100}  = 418 x (2.67-1 ) x (0.4/1000 m) x {((3x15.556)+70)/100}

Vs = 0.3258 m/sec

Velocity for medium sand (0.4 mm) is 0.3258 m/sec.....................(Answer)

Fall = h = 6" = 0.1524 meter

6" Fall time =t = h/Vs = 0.1524 m / 0.3258 m/sec = 0.468 second........................(Answer)

(c)

=>

Very fine sand diameter d3 =0.075 mm

SG of fine sand = G3 = 2.70

Water Temparature = T =60°F = { (60°F − 32) × 5/9 } = 15.556°C

Partical diameter =d3 = 0.075 mm ,   < 0.1 mm

Settling velocity = Vs =418 (G-1 ) d^2 {(3T+70)/100}  = 418 x (2.70-1 ) x (0.075/1000 m)^2 x {((3x15.556)+70)/100}

Vs = 4.663 x 10^-6 m/sec

Velocity for very fine sand (0.075 mm) is 4.663 x 10^-6 m/sec.....................(Answer)

Fall = h = 6" = 0.1524 meter

6" Fall time =t = h/Vs = 0.1524 m / 4.663 x 10^-6 m/sec = 32680 second. = 9 hours 4 minuts 40 Second....(Answer)

(d)

=>

Clay particals diameter d4 = 0.001 mm

SG of clay = G4 = 2.8

Water Temparature = T =60°F = { (60°F − 32) × 5/9 } = 15.556°C

Partical diameter =d4 = 0.001 mm ,   < 0.1 mm

Settling velocity = Vs =418 (G-1 ) d^2 {(3T+70)/100}  = 418 x (2.80-1 ) x (0.001/1000 m)^2 x {((3x15.556)+70)/100}

Vs = 8.778 x 10^-10 m/sec

Velocity for clay (0.001 mm) is 8.778 x 10^-10 m/sec.....................(Answer)

Fall = h = 6" = 0.1524 meter

6" Fall time =t = h/Vs = 0.1524 m / 8.778 x 10^-10 m/sec = 173613873 second

= 5.50526 years ........................(Answer)


Related Solutions

(a) Calculate the settling velocity of glass spheres (density = 2467 kg/m3) having diameter as 1.5...
(a) Calculate the settling velocity of glass spheres (density = 2467 kg/m3) having diameter as 1.5 mm in water. The slurry contains 65% by weight solid. Use Newton’s law. (b) Mixture of an ore (density 2000 kg/m3) and gangue (density 7000 kg/m3) is to be separated in a hydraulic elutriator. The mixture has following size distribution, which is valid for ore as well as gangue. Predict the upward velocity of water in elutriator so that entire ore is collected in...
Apply the discrete particle settling theory to calculate the terminal settling velocity of a sand particle...
Apply the discrete particle settling theory to calculate the terminal settling velocity of a sand particle in the water at 25°C having a particle diameter of 300 µm and a density of 2,450 kg/m3. Show the calculations and logic for at least two of your iterations. please clear steps
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 sand particle has an average diameter of 1 mm and a shape factor of 0.90...
A sand particle has an average diameter of 1 mm and a shape factor of 0.90 and a specific gravity of 2.1, determine the terminal velocity of the particle settling in water at 20oC (kinematic viscosity of water = 1.003 x 10-6 m2/s and specific gravity = 1) Drag coefficient can be computed using the formula: Cd= 24/Re +( 3/sqrtRe ) + 0.34   Answer: 0.1419 m/s
The sediment settling velocity, ωs (ms-1) in stagnant water is dependent on the sediment diameter, d...
The sediment settling velocity, ωs (ms-1) in stagnant water is dependent on the sediment diameter, d (m), sediment density, ρs (kgm-3), water density, ρ (kgm-3),dynamic viscosity of water, μ (kgm-1 s-1), and gravitational acceleration, g (ms-2).By applying the dimensional analysis, develop the equation in terms of phi, π to explain the ωs.
A packed bed reactor is filled with catalyst material with a diameter of 1.5 mm. The...
A packed bed reactor is filled with catalyst material with a diameter of 1.5 mm. The length of the reactor is 80 cm and the catalyst has a porosity of 0.45. The superficial mass velocity of the inlet gas is 7.5 kg/m2-s with a viscosity of 1.55x10-5 kg/m-s and a density of 2.8 kg/m3. The inlet pressure is 300 kPa. Find the pressure, P, at the end (the exit) of the PBR.
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...
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 jet of water 50 mm in diameter with a velocity of 20 m/s strikes a...
A jet of water 50 mm in diameter with a velocity of 20 m/s strikes a flat plate inclined at an angle of 30° to the axis of the jet. Determine (i) the normal force exerted on the plate when the plate is stationary (ii) the normal force exerted on the plate when the plate is moving at 5 m/s in the direction of the jet (iii) the work-done on the plate and the efficiency for case (ii).
ADVERTISEMENT
ADVERTISEMENT
ADVERTISEMENT