SOLUTIONS TO CHAPTER 3: MULTIPLE PARTICLE SYSTEMS EXERCISE 3.1 A suspension in water of uniformly sized spheres of diameter 100 μm and density 1200 kg/m3 has a solids volume fraction of 0.2. The suspension settles to a bed of solids volume fraction 0.5. (For water: density, 1000 kg/m3 and viscosity, 0.001 Pas) The single particle terminal velocity of the spheres in water may be taken as 1.1mm/s. Calculate: a) The velocity at which the clear water/suspension interface settles; b) The velocity at which the sediment/suspension interface rises. SOLUTION TO EXERCISE 3.1 (a) Solids concentration of initial suspension, CB = 0.20 Text-Equation 3.28 allows us to calculate the velocity of interfaces between suspensions of different concentrations: The velocity of the interface between initial suspension (B) and clear liquid (A) is therefore:

Uint,AB =UpACA − UpBCB

CA − CB

Since CA = 0, the equation reduces to U int,AB = UpB

UpB is the hindered settling velocity of particles relative to the vessel wall in batch settling and is given by Text-Equation 3.24: Up = UTεn

To check whether Stokes Law is valid, we calculate the single particle Reynolds number at the terminal velocity:

Rep =(100 ×10−6) ×1.1 ×10−3 ×1000

0.001= 0.11

This value is less than the limiting value for Stokes Law (0.3) and so Stokes Law applies and therefore in Text-Equation 3.24 exponent n = 4.65. The voidage of the initial suspension, εΒ = 1 - CB = 0.80

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hence, U pB = 1.1 ×10−3 × 0.804.65

= 3.897 x 10-4 m/s Hence, the velocity of the interface between the initial suspension and the clear liquid is 0.39 mm/s. The fact that the velocity is positive indicates that the interface is moving downwards. (b) Here again we apply Text-Equation 3.28 to calculate the velocity of interfaces between suspensions of different concentrations: The velocity of the interface between initial suspension (B) and sediment (S) is therefore:

Uint,BS =UpBCB − UpSCS

CB − CS

With CB = 0.20 and CS = 0.50 and since the velocity of the sediment, UpS is zero, we have:

Uint,BS =UpB0.20 − 00.20 − 0.50

= −0.6667UpB

And from part (a), we know that UpB = 0.39mm/s, and so Uint,BS = −0.26 mm / s

The negative sign signifies that the interface is moving upwards. So, the interface between initial suspension and sediment is moving upwards at a velocity of 0.26mm/s. EXERCISE 3.2 A height-time curve for the sedimentation of a suspension in a vertical cylindrical vessel is shown in Text-Figure 3.E2.1. The initial solids concentration of the suspension is 150 kg/m3. Determine: a) The velocity of the interface between clear liquid and suspension of concentration 150 kg/m3. b) The time from the start of the test at which the suspension of concentration 240 kg/m3 is in contact with the clear liquid. c) The velocity of the interface between the clear liquid and suspension of concentration 240 kg/m3.

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d) The velocity at which a layer of concentration 240 kg/m3 propagates upwards from the base of the vessel. e) The concentration of the final sediment. SOLUTION TO EXERCISE 3.2 (a) Since the initial suspension concentration is 150 kg/m3, the velocity required in this question is the velocity of the AB interface. This is given by the slope of the straight portion of the height-time curve.

Slope = 0 − 80

27.5 − 0= −2.91 cm / s (the negative sign indicates downwards)

Therefore, velocity of the interface between clear liquid and suspension of concentration 150 kg/m3 is 2.91 cm/s downwards. (b) We must first find the point on the curve corresponding to the point at which a suspension of concentration 240 kg/m3 interfaces with the clear suspension. From Equation 3.38, with C = 240, CB = 150 and h0 = 80 cm, we find: h1 =

150 ×80240

= 50 cm

A line drawn through the point t = 0, h = h1 tangent to the curve locates the point on the curve corresponding to the time at which a suspension of concentration 240 kg/m3 interfaces with the clear suspension (Solution Manual-Figure 3.2.1). The coordinates of this point are t = 22 sec, h = 33 cm. (c) The velocity of this interface is the slope of the curve at this point: slope of curve at 22 sec, 33 cm =−0.77 cm / s downward velocity of interface = 0.77 cm/s (d) From the consideration above, after 22 seconds the layer of concentration 240 kg/m3 has just reached the clear liquid interface and has travelled a distance of 33 cm from the base of the vessel in this time. Therefore, upward propagation velocity of this layer = h

t=

3323

=1.5 cm / s

(e) To find the concentration of the final sediment we again use Equation 3.38. The value of h1 corresponding to the final sediment (h1S) is found by drawing a tangent to

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.3

the part of the curve corresponding to the final sediment and projecting it to the h axis. In this case h1S = 20 cm and so from Text-Equation 3.38,

final sediment concentration, C=C0h0h1S

=150 × 80

20= 600 kg / m3

EXERCISE 3.3 A suspension in water of uniformly sized spheres of diameter 90 μm and density 1100 kg/m3 has a solids volume fraction of 0.2. The suspension settles to a bed of solids volume fraction 0.5. (For water: density, 1000 kg/m3 and viscosity, 0.001 Pas) The single particle terminal velocity of the spheres in water may be taken as 0.44mm/s. Calculate: a) The velocity at which the clear water/suspension interface settles; b) The velocity at which the sediment/suspension interface rises. SOLUTION TO EXERCISE 3.3 (a) Solids concentration of initial suspension, CB = 0.20 Text-Equation 3.28 allows us to calculate the velocity of interfaces between suspensions of different concentrations: The velocity of the interface between initial suspension (B) and clear liquid (A) is therefore:

Uint,AB =UpACA − UpBCB

CA − CB

Since CA = 0, the equation reduces to Uint,AB = UpB

UpB is the hindered settling velocity of particles relative to the vessel wall in batch settling and is given by Text-Equation 3.24: Up = UTεn

To check whether Stokes Law is valid, we calculate the single particle Reynolds number at the terminal velocity:

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.4

Rep =(90 ×10−6) × 0.44 ×10−3 ×1000

0.001= 0.0396

This value is less than the limiting value for Stokes Law (0.3) and so Stokes Law applies and therefore in Text-Equation 3.24 exponent n = 4.65. The voidage of the initial suspension, εΒ = 1 - CB = 0.80 hence, U pB = 0.44 ×10−3 × 0.804.65

= 1.56 x 10-4 m/s Hence, the velocity of the interface between the initial suspension and the clear liquid is 0.156 mm/s. The fact that the velocity is positive indicates that the interface is moving downwards. (b) Here again we apply Text-Equation 3.28 to calculate the velocity of interfaces between suspensions of different concentrations: The velocity of the interface between initial suspension (B) and sediment (S) is therefore:

Uint,BS =UpBCB − UpSCS

CB − CS

With CB = 0.20 and CS = 0.50 and since the velocity of the sediment, UpS is zero, we have:

Uint,BS =UpB0.20 − 00.20 − 0.50

= −0.6667UpB

And from part (a), we know that UpB = 0.156 mm/s, and so Uint,BS = −0.104 mm / s

The negative sign signifies that the interface is moving upwards. So, the interface between initial suspension and sediment is moving upwards at a velocity of 0.104mm/s. EXERCISE 3.4 A height-time curve for the sedimentation of a suspension in a vertical cylindrical vessel is shown in Text-Figure 3.E2.1. The initial solids concentration of the suspension is 200 kg/m3. Determine:

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a) The velocity of the interface between clear liquid and suspension of concentration 200 kg/m3. b) The time from the start of the test at which the suspension of concentration 400 kg/m3 is in contact with the clear liquid. c) The velocity of the interface between the clear liquid and suspension of concentration 400 kg/m3. d) The velocity at which a layer of concentration 400 kg/m3 propagates upwards from the base of the vessel. e) The concentration of the final sediment. SOLUTION TO EXERCISE 3.4 (a) Since the initial suspension concentration is 200 kg/m3, the velocity required in this question is the velocity of the AB interface. This is given by the slope of the straight portion of the height-time curve (Solution Manual-Figure 3.4.1).

Slope = 0 − 80

27.5 − 0= −2.91 cm / s (value given in book is incorrect)

Therefore, velocity of the interface between clear liquid and suspension of concentration 200 kg/m3 is 2.91 cm/s downwards. (b) We must first find the point on the curve corresponding to the point at which a suspension of concentration 400 kg/m3 interfaces with the clear suspension. From Equation 3.38, with C = 400, CB = 200 and h0 = 80 cm, we find: h1 =

200 ×80400

= 40 cm

A line drawn through the point t = 0, h = h1 tangent to the curve locates the point on the curve corresponding to the time at which a suspension of concentration 240 kg/m3 interfaces with the clear suspension (Solution Manual-Figure 3.4.1). The coordinates of this point are t = 32.5 sec, h = 27.5 cm. (c) The velocity of this interface is the slope of the curve at this point: slope of curve at 32.5 sec, 27.5 cm =−0.40 cm / s

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downward velocity of interface = 0.4 cm/s (d) From the consideration above, after 32.5 seconds the layer of concentration 400 kg/m3 has just reached the clear liquid interface and has travelled a distance of 27.5 cm from the base of the vessel in this time.

Therefore, upward propagation velocity of this layer =ht

=27.532.5

= 0.846 cm / s

(e) To find the concentration of the final sediment we again use Text-Equation 3.38. The value of h1 corresponding to the final sediment (h1S) is found by drawing a tangent to the part of the curve corresponding to the final sediment and projecting it to the h axis. In this case h1S = 20 cm and so from Text-Equation 3.38,

final sediment concentration, C=C0h0h1S

=200 × 80

20= 800 kg / m3

EXERCISE 3.5 a) Spherical particles of uniform diameter, 40 μm and particle density 2000 kg/m3 form a suspension of solids volume fraction 0.32 in a liquid of density 880 kg/m3 and viscosity 0.0008 Pas. Assuming Stokes Law applies, calculate (i) the sedimentation velocity and (ii) the sedimentation volumetric flux for this suspension. (b) A height-time curve for the sedimentation of a suspension in a cylindrical vessel is shown in Text-Figure 3.E5.1. The initial concentration of the suspension for this test is 0.12 m3/m3. Calculate: (i) the velocity of the interface between clear liquid and a suspension of concentration, 0.12 m3/m3. (ii) the velocity of the interface between clear liquid and a suspension of concentration 0.2 m3/m3. (iii) the velocity at which a layer of concentration, 0.2 m3/m3 propagates upwards from the base of the vessel. (iv) the concentration of the final sediment.

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(v) the velocity at which the sediment propagates upwards from the base. SOLUTION TO EXERCISE 3.5 Part (a) (i) Solids concentration of initial suspension, CB = 0.32 Text-Equation 3.28 allows us to calculate the velocity of interfaces between suspensions of different concentrations: The velocity of the interface between initial suspension (B) and clear liquid (A) is therefore:

Uint,AB =UpACA − UpBCB

CA − CB

Since CA = 0, the equation reduces to Uint,AB = UpB

UpB is the hindered settling velocity of particles relative to the vessel wall in batch settling and is given by Text-Equation 3.24: Up = UTεn

Assuming Stokes Law applies, then n = 4.65 and the single particle terminal velocity is given by Text-Equation 2.13 (see Chapter 2 - Single Particles in Fluids):

UT =x2 (ρp − ρf )g

18μ

⎛

⎝ ⎜

⎞

⎠ ⎟

UT =9.81× (40 ×10−6 )2 × (2000 − 880)

18 × 0.0008

= 1.221 x 10-3 m/s To check that assumption of Stokes Law is valid, we calculate the single particle Reynolds number:

Rep =(40 ×10−6) ×1.221 ×10−3 × 880

0.0008= 0.054

This value is less than the limiting value for Stokes Law (0.3) and so the assumption is valid. Hence in Text-Equation 3.24, exponent n = 4.65.

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The voidage of the initial suspension, εΒ = 1 - CB = 0.68 hence, U pB = 1.221 ×10−3 × 0.684.65

= 2.03 x 10-4 m/s Hence, the velocity of the interface between the initial suspension and the clear liquid is 0.203 mm/s. The fact that the velocity is positive indicates that the interface is moving downwards. (ii) From Text-Equation 3.15, sedimentation volumetric flux, Ups = Up 1 − ε( )

Hence, with Up = 0.203 mm/s and ε = 0.68, volumetric flux, U ps = 0.203 × 1 − 0.68( ) = 0.065 mm3 / mm2

Part (b) (i) Since the initial suspension concentration is 0.12 m3/m3, the velocity required in this question is the velocity of the AB interface. This is given by the slope of the straight portion of the height-time curve (Solution Manual-Figure 3.5.1).

Slope = 25 − 5022.5 − 0

= −1.11 cm / s (the negative sign indicates downwards)

Therefore, the velocity of the interface between clear liquid and a suspension of concentration, 0.12 m3/m3 is 1.11 cm/s downwards. (ii) We must first find the point on the curve corresponding to the point at which a suspension of concentration 0.2 m3/m3 interfaces with the clear suspension. From Text-Equation 3.38, with C = 0.2, CB = 0.12 and h0 = 50 cm, we find:

h1 =0.12 × 50

0.2= 30 cm

A line drawn through the point t = 0, h = h1 tangent to the curve locates the point on the curve corresponding to the time at which a suspension of concentration 0.2 m3/m3 interfaces with the clear suspension (Solution Manual-Figure 3.5.1). The coordinates of this point are t = 35 sec, h = 18 cm. (iii) The velocity of this interface is the slope of the curve at this point: slope of curve at 35 sec, 18 cm =−0.35 cm / s downward velocity of interface = 0.35 cm/s

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(iv) From the consideration above, after 35 seconds the layer of concentration 0.2 m3/m3 has just reached the clear liquid interface and has travelled a distance of 18 cm from the base of the vessel in this time.

Therefore, upward propagation velocity of this layer =ht

=1835

= 0.514 cm / s

(v) To find the concentration of the final sediment we again use Text-Equation 3.38. The value of h1 corresponding to the final sediment (h1S) is found by drawing a tangent to the part of the curve corresponding to the final sediment and projecting it to the h axis (Solution Manual-Figure 3.5.1). In this case h1S = 15 cm and so from Text-Equation 3.38,

final sediment concentration, C=C0h0h1S

=0.12 × 50

15= 0.4 m3 / m3

(vi) At the end of the test (ts), we know that the surface of the sediment has risen from

h = 0 to h = h1S in a time ts. Hence sediment velocity = h1StS

=1550

= 0.3 cm / s

EXERCISE 3.6 A height-time curve for the sedimentation of a suspension in a vertical cylindrical vessel is shown in Text-Figure 3.E6.1. The initial solids concentration of the suspension is 100 kg/m3. Determine: a) the velocity of the interface between clear liquid and suspension of concentration 100 kg/m3. b) the time from the start of the test at which the suspension of concentration 200 kg/m3 is in contact with the clear liquid. c) the velocity of the interface between the clear liquid and suspension of concentration 200 kg/m3. d) the velocity at which a layer of concentration 200 kg/m3 propagates upwards from the base of the vessel. e) the concentration of the final sediment.

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SOLUTION TO EXERCISE 3.6 (a) Since the initial suspension concentration is 100 kg/m3, the velocity required in this question is the velocity of the AB interface. This is given by the slope of the straight portion of the height-time curve. Slope= −0.67 cm / s (negative sign indicates downwards) Therefore, the velocity of the interface between clear liquid and suspension of concentration 100 kg/m3 is 0.67 cm/s downwards. (b) We must first find the point on the curve corresponding to the point at which a suspension of concentration 200 kg/m3 interfaces with the clear suspension. From Equation 3.38, with C = 200, CB = 100 and h0 = 80 cm, we find:

h1 =100 ×80

200= 40 cm

A line drawn through the point t = 0, h = h1 tangent to the curve locates the point on the curve corresponding to the time at which a suspension of concentration 200 kg/m3 interfaces with the clear suspension (Solution Manual-Figure 3.6.1). The coordinates of this point are t = 140 sec, h = 26.5 cm. (c) The velocity of this interface is the slope of the curve at this point: slope of curve at 140 sec, 26.5 cm =−0.98 cm / s downward velocity of interface = 0.98 cm/s (d) From the consideration above, after 140 seconds the layer of concentration 200 kg/m3 has just reached the clear liquid interface and has travelled a distance of 26.5 cm from the base of the vessel in this time.

Therefore, upward propagation velocity of this layer =ht

=26.5140

= 0.189 cm / s

(e) To find the concentration of the final sediment we again use Text-Equation 3.38. The value of h1 corresponding to the final sediment (h1S) is found by drawing a tangent to the part of the curve corresponding to the final sediment and projecting it to the h axis. In this case h1S = 20 cm and so from Text-Equation 3.38,

final sediment concentration, C=C0h0h1S

=100 × 80

20= 400 kg / m3

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EXERCISE 3.7 A suspension in water of uniformly sized spheres of diameter 80 μm and density 1300 kg/m3 has a solids volume fraction of 0.10. The suspension settles to a bed of solids volume fraction 0.4. (For water: density, 1000 kg/m3 and viscosity, 0.001 Pas) The single particle terminal velocity of the spheres under these conditions is 1.0 mm/s. Calculate: a) The velocity at which the clear water/suspension interface settles b) The velocity at which the sediment/suspension interface rises. SOLUTION TO EXERCISE 3.7 (a) Solids concentration of initial suspension, CB = 0.10 Text-Equation 3.28 allows us to calculate the velocity of interfaces between suspensions of different concentrations: The velocity of the interface between initial suspension (B) and clear liquid (A) is therefore:

Uint,AB =UpACA − UpBCB

CA − CB

Since CA = 0, the equation reduces to Uint,AB = UpB

UpB is the hindered settling velocity of particles relative to the vessel wall in batch settling and is given by Text-Equation 3.24: Up = UTεn

To check whether Stokes Law is valid, we calculate the single particle Reynolds number at the terminal velocity:

Rep =xUTρf

μ=

(80 ×10−6) ×1.0 ×10−3 ×10000.001

= 0.08

This value is less than the limiting value for Stokes Law (0.3) and so Stokes Law applies and therefore, in Text-Equation 3.24, exponent n = 4.65.

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The voidage of the initial suspension, εΒ = 1 - CB = 0.90 hence, U pB = 1.0 ×10−3 × 0.904.65

= 6.13 x 10-4 m/s Hence, the velocity of the interface between the initial suspension and the clear liquid is 0.613 mm/s. The fact that the velocity is positive indicates that the interface is moving downwards. (b) Here again we apply Text-Equation 3.28 to calculate the velocity of interfaces between suspensions of different concentrations: The velocity of the interface between initial suspension (B) and sediment (S) is therefore:

Uint,BS =UpBCB − UpSCS

CB − CS

With CB = 0.10 and CS = 0.40 and since the velocity of the sediment, UpS is zero, we have:

Uint,BS =UpB0.10 − 00.10 − 0.40

= −0.3333UpB

And from part (a), we know that UpB = 0.613 mm/s, and so Uint,BS = −0.204 mm / s

The negative sign signifies that the interface is moving upwards. So, the interface between initial suspension and sediment is moving upwards at a velocity of 0.204 mm/s. EXERCISE 3.8 A height-time curve for the sedimentation of a suspension in a vertical cylindrical vessel is shown in Text-Figure 3.E6.1. The initial solids concentration of the suspension is 125 kg/m3. Determine: a) the velocity of the interface between clear liquid and suspension of concentration 125 kg/m3. b) the time from the start of the test at which the suspension of concentration 200 kg/m3 is in contact with the clear liquid.

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c) the velocity of the interface between the clear liquid and suspension of concentration 200 kg/m3. d) the velocity at which a layer of concentration 200 kg/m3 propagates upwards from the base of the vessel. e) the concentration of the final sediment. SOLUTION TO EXERCISE 3.8 (a) Since the initial suspension concentration is 125 kg/m3, the velocity required in this question is the velocity of the AB interface. This is given by the slope of the straight portion of the height-time curve (Solution Manual-Figure 3.8.1). Slope = -0.67 cm / s (negative sign indicates downwards) Therefore, the velocity of the interface between clear liquid and suspension of concentration 125 kg/m3 is 0.67 cm/s downwards. (b) We must first find the point on the curve corresponding to the point at which a suspension of concentration 200 kg/m3 interfaces with the clear suspension. From Text-Equation 3.38, with C = 200, CB = 125 and h0 = 80 cm, we find:

h1 =125 × 80

200= 50 cm

A line drawn through the point t = 0, h = h1 tangent to the curve locates the point on the curve corresponding to the time at which a suspension of concentration 200 kg/m3 interfaces with the clear suspension (Solution Manual-Figure 3.8.1). The coordinates of this point are t = 80 sec, h = 35 cm. (c) The velocity of this interface is the slope of the curve at this point: slope of curve at 80 sec, 35 cm =−0.19 cm / s downward velocity of interface = 0.19 cm/s (d) From the consideration above, after 80 seconds the layer of concentration 200 kg/m3 has just reached the clear liquid interface and has travelled a distance of 35 cm from the base of the vessel in this time.

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Therefore, upward propagation velocity of this layer =ht

=3580

= 0.4375 cm / s

(e) To find the concentration of the final sediment we again use Text-Equation 3.38. The value of h1 corresponding to the final sediment (h1S) is found by drawing a tangent to the part of the curve corresponding to the final sediment and projecting it to the h axis. In this case h1S = 20 cm and so from Text-Equation 3.38,

final sediment concentration, C=C0h0h1S

=125 × 80

20= 500 kg / m3

EXERCISE 3.9 Use the batch flux plot in Text-Figure 3.E9.1 to answer the following questions (Note that the sediment concentration is 0.44 volume fraction). (i) Determine the range of initial suspension concentration over which a variable concentration zone is formed under batch settling conditions. (ii) For a batch settling test using a suspension with an initial concentration 0.18 volume fraction and initial height 50cm, determine the settling velocity of the interface between clear liquid and suspension of concentration 0.18 volume fraction. (iii) Determine the position of this interface 20 minutes after the start of this test. (iv) Produce a sketch showing the concentration zones in the settling test 20 minutes after the start of this test. SOLUTION TO EXERCISE 3.9 (a) Determine the range on initial suspension concentrations by drawing a line through the point C = CS = 0.44, Ups = 0 tangent to the inflection point in the batch flux curve. This is shown as line XCS in Solution Manual-Figure 3.9.1. The range of initial suspension concentrations for which a zone of variable concentration is formed in batch settling (type 2 settling) is defined by CBmin and CBmax. CBmin is the value of C at which the line XCS intersects the settling curve and CBmax is the value of C at the tangent to the inflection point. From Solution Manual-Figure 32.9.1, we see that CBmin = 0.135 and CBmax = 0.318.

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(b) To calculate the concentration profile we must first determine the velocities of the interfaces between the zones A, B, E and S and hence find their positions after 20 minutes. The line AB in Solution Manual-Figure 3.9.1 joins the point representing A the clear liquid (0, 0) and the point B representing the initial suspension (0.18, Ups). The slope of line AB is equal to the velocity of the interface between zones A and B. From Figure 2.9.1, Uint,AB = +0.1333 mm / s or + 0.80 cm/min

The slope of the line from point B tangent to the curve is equal to the velocity of the interface between the initial suspension B and the minimum value of the variable concentration zone Emin. From Solution Manual-Figure 3.9.1, Uint,BE min = −0.104 mm / s or - 0.626 cm/min.

The slope of the line tangent to the curve and passing through the point representing the sediment (point C = CS = 0.44, Ups = 0) is equal to the velocity of the interface between the maximum value of the variable concentration zone CEmax and the sediment. From Solution Manual-Figure 3.9.1, Uint,E max S = −0.082 mm / s or - 0.49 cm/min.

Therefore, after 20 minutes the distances travelled by the interfaces will be: AB interface 16 cm (0.80 x 20) downwards BEmin interface 12.5 cm (0.626 x 20) upwards EmaxS interface 9.8 cm (0.49 x 20) upwards Therefore the positions of the interfaces (distance from the base of the test vessel) after 20 minutes will be: AB interface 34 cm BEmin interface 12.5 cm EmaxS interface 9.8 cm From Solution Manual-Figure 3.9.1 we determine the minimum and maximum values of suspension concentration in the variable zone: CEmin = 0.30 CEmax = 0.318

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Using this information we can plot the concentration profile in the test vessel 20 minutes after the start of the test. A sketch of the profile is shown in Solution Manual-Figure 3.9.2. The shape of the concentration profile within the variable concentration zone may be determined by the following method. Recalling that the slope of the batch flux plot (Text-Figure 3.E3.1) at a value of suspension concentration C is the velocity of a layer of suspension of that concentration, we find the slope at two or more values of concentration and then determine the positions of these layers after 20 minutes. This allows us to determine the shape of the profile within the zone of variable concentration. EXERCISE 3.10 Consider the batch flux plot shown in Worked Example 3.3 (Figure 3.W3.1). Given that the final sediment concentration is 0.36 volume fraction, (a) Determine the range of initial suspension concentration over which a variable concentration zone is formed under batch settling conditions. (b) Calculate and sketch the concentration profile after 40 minutes of the batch settling test with an initial suspension concentration of 0.08 and an initial height of 100cm. (c) Estimate the height of the final sediment and the time at which the test is complete. SOLUTION TO EXERCISE 3.10 (a) Determine the range on initial suspension concentrations by drawing a line through the point C = CS = 0.36, Ups = 0 tangent to the inflection point in the batch flux curve. This is shown as line XCS in Solution Manual-Figure 3.10.1. The range of initial suspension concentrations for which a zone of variable concentration is formed in batch settling (type 2 settling) is defined by CBmin and CBmax. CBmin is the value of C at which the line XCS intersects the settling curve and CBmax is the value of C at the tangent to the inflection point. From Solution Manual-Figure 3.10.1, we see that CBmin = 0.045 and CBmax = 0.20. (b) To calculate the concentration profile we must first determine the velocities of the interfaces between the zones A, B, E and S and hence find their positions after 40 minutes.

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The line AB in Solution Manual-Figure 3.10.1 joins the point representing A the clear liquid (0, 0) and the point B representing the initial suspension (0.08, Ups). The slope of line AB is equal to the velocity of the interface between zones A and B. From Solution Manual-Figure 3.10.1, Uint,AB = +0.2075 mm / s or + 1.245 cm/min

The slope of the line from point B tangent to the curve is equal to the velocity of the interface between the initial suspension B and the minimum value of the variable concentration zone Emin. From Solution Manual-Figure 3.10.1, Uint,BE min = −0.085 mm / s or - 0.51 cm/min.

The slope of the line tangent to the curve and passing through the point representing the sediment (point C = CS = 0.36, Ups = 0) is equal to the velocity of the interface between the maximum value of the variable concentration zone CEmax and the sediment. From Solution Manual-Figure 3.10.1, Uint,E max S = −0.043 mm / s or - 0.26 cm/min.

Therefore, after 40 minutes the distances travelled by the interfaces will be: AB interface 49.8 cm (1.245 x 40) downwards BEmin interface 20.4 cm (0.51 x 40) upwards EmaxS interface 10.4 cm (0.26 x 40) upwards Therefore the positions of the interfaces (distance from the base of the test vessel) after 40 minutes will be: AB interface 50.2 (100 - 49.8) cm BEmin interface 20.4 cm EmaxS interface 10.4 cm From Solution Manual-Figure 3.10.1 we determine the minimum and maximum values of suspension concentration in the variable zone: CEmin = 0.17 CEmax = 0.20 Using this information we can plot the concentration profile in the test vessel 40 minutes after the start of the test. A sketch of the profile is shown in Solution Manual-Figure 3.10.2. The shape of the concentration profile within the variable

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.18

concentration zone may be determined by the following method. Recalling that the slope of the batch flux plot at a value of suspension concentration C is the velocity of a layer of suspension of that concentration, we find the slope at two or more value of concentration and then determine the positions of these layers after 40 minutes. These points are plotted on the concentration profile in order to determine the shape of the profile within the zone of variable concentration. The time for the end of the test is found in the following way. The end of the test is when the position of the EmaxS interface coincides with the height of the final sediment. The height of the final sediment may be found using Text-Equation 3.38 [see part (iv) of Worked Example 3.1]: CShS = CBh0

where hS is the height of the final sediment and h0 is the initial height of the suspension (at the start of the test). With CS = 0.36, CB = 0.08 and h0 = 100cm, we find that hS = 22.2 cm. The velocity of the sediment interface with the variable concentration zone was found above to be 0.26 cm/min upw E max S ).

Hence the test ends when the sediment interface has travelled a distance hS at thi

ards

s

i.e. time to end of test =

(Uint,

velocity: hS

Uint,E max S=

22.20.26

= 85.5 minutes

EXERCISE 3.11 The batch and continuous flux plots supplied in Text-Figure 3.E11.1 are for a thickener of area 200m2 handling a feed rate of 0.04m3/s and an underflow rate of .025m3/s.

s, graphically determine the critical or limiting feed concentration for

trations in the verflow, underflow, in the regions above and below the feed well.

once ration in the overflow and the steady state has been reached.

0 Using these plotthis thickener. If the feed concentration is 0.18 m3/m3, determine the solids conceno Under the same flow rate conditions in the same thickener, the feed concentration increases to 0.24. Estimate the new solids c ntunderflow once

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.19

SOLUTION TO EXERCISE 3.11:

nderflow rate, L = 0.025 m3/s

aterial balance gives, underflow rate, V = F - L = 0.015 m3/s

xpressing these flows s fluxes based on the thickener area (A = 200 m2):

Part (a) Feed rate, F = 0.04 m3/s U M E a

FA

= 0.2 mm / s

LA

= 0.125 mm / s

AV

= 0.075 mm / s

The variation in fluxes with concentration of the suspension are then:

Feed flux = CFFA

⎛ ⎝

⎞ ⎠

Flux in underflow = CLLA

⎛ ⎝

⎞ ⎠

Flux in overflow = CVVA

⎛ ⎝

⎞ ⎠

Lines of slope F/A, L/A and -V/A drawn on the flux plot represent the fluxes in the feed, underflow and overflow respectively (Solution Manual-Figure 3.11.1). The total flux plot for the section below the feed point is found by adding batch flux plot to the underflow flux line (this has already been done in Solution Manual-Figure 3.11.1). The total flux plot for the section above the feed point is found by adding the batch flux plot to the underflow flux line (which is negative since it is an upward flux) (this has also already been done in Solution Manual-Figure 3.11.1). These plots are shown

Solution Manual-Figure 3.11.1.

ution Manual-Figure 3.11.1). The corresponding feed concentration CFcrit = 0.21.

he corresponding concentration in the downflow section, CB is also 0.21.

d where the critical flux line tersects the underflow flux line. This gives CL = 0.34.

in In this case the total flux curve has a minimum in it and so this corresponds to the maximum flux that the downflow section can take. The critical feed flux is therefore 0.041 mm/s (Solis T The corresponding concentration in the underflow is founin

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.20

Part (b): Referring again to Solution Manual-Figure 3.11.1, if the feed flux is increased to 0.18, we see that the corresponding feed flux is about 0.036 mm/s. The thickener is underloaded since the feed concentration is less than the critical value. All the feed passes through the downflow section giving a concentration CB = 0.087 (where constant flux 0.036 intersects the total down flux curve) and an underflow concentration CL = 0.29 (where the constant flux 0.036 intersect the underflow line). The concentration in the upward flow section CT and the overflow concentration CV re both zero.

on, CT = 0.24 and a corresponding concentration, CV = 0.08 in the verflow.

ell and the point of underflow withdrawal (neglect the conical base f the thickener).

able

a (c) Referring to Solution Manual-Figure 3.11.1, if the feed flux is increased to 0.24, the thickener is now overloaded and we see that the corresponding feed flux is about 0.048 mm/s. At this feed concentration the downflow section is only able to take a flux of 0.042 mm/s and gives an underflow concentration, CL = 0.34. The excess flux of 0.006 mm/s passes into the upflow section. This flux in the upflow section gives a concentratio EXERCISE 3.12 (a) Using the batch flux plot data given in Text-Table 3.E12.1, graphically determine the limiting feed concentration for a thickener of area 300 m2 handling a feed rate of 0.03 m3/s and with an underflow rate of 0.015 m3/s. Determine the underflow concentration and overflow concentration under these conditions. Sketch a possible concentration profile in the thickener clearly indicating the positions of the overflow launder, the feed wo T 3.E12.1: Batch flux test data for Exercise 3.12

C 0.01 0.02 0.04 0.06 0.08 0.10 0.12 0.14 0.16 0.18 0.20Flux mm/s (x 103)

5.0 9.1 13.6 15.7 16.4 16.4 15.7 13.3 10.0 8.3 7.3

C 0.22 0.24 0.26 0.28 0.30 0.32 0.34 0.36 0.38 0.40

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.21

Flux 6.7 5.6 5.1 4.5 4.2 3.8 3.5 3.3 3.0 2.9 mm/s (x 103) (b) Under the same flow conditions as above, the concentration in the feed increases

110% of the limiting value. Estimate the solids concentration in the overflow, in hickener above the feed well and in the section

e feed well.

CISE 3.12: art (a)

first plotted with concentration as abscissa (see Solution

nderflow rate, L = 0.015 m3/s

aterial balance gives nderflow rate, V = F - L = 0.015 m3/s

Expressing these flows as fluxes based on the thickener area (A = 300 m2):

tothe underflow, in the section of the tbelow th SOLUTION TO EXERPThe batch flux data is Manual-Figure 3.12.1). Feed rate, F = 0.03 m3/s U M , u

FA

= 0.1 mm / s

L

= 0.05 mm / s AVA

= 0.05 mm / s

The variations in fluxes with concentration of the suspension are then:

Feed flux = CFFA

⎛ ⎝

⎞ ⎠

Flux in underflow = CLLA

⎛ ⎝

⎞ ⎠

Flux in overflow = CVVA

⎛ ⎝

⎞ ⎠

Lines of slope F/A, L/A and -V/A drawn on the flux plot represent the fluxes in the feed, underflow and overflow respectively (Solution Manual-Figure 3.12.1). The total flux plot for the section below the feed well is found by adding batch flux plot to the nderflow flux line. The total flux plot for the section above the feed well is found by u

adding the batch flux plot to the overflow flux line (which is negative since it is an upward flux). These plots are shown in Solution Manual-Figure 3.12.1.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.22

In this case the total flux curve has a minimum in it and so this corresponds to the

ed concentration

ope L/A). This gives CL = 0.34. here are two possible concentrations in the downflow section which could give rise

ical flux (0.017 mm/s); these are CBmin = 0.05 and CBmax = 0.19.

that this xcess flux gives rise to a concentration above the feed well of CT = 0.19 and an

ion of CV = 0.034. Passing through the downflow section below ion

uid of density 1000 kg/m3 and viscosity 0.002 Pas. The resulting spension has a solids volume fraction of 0.30.

liquid may be taken as the clear water/suspension

terface settles.

) Solids concentration of initial suspension, CB = 0.30

ion 3.28 allows us to calculate the velocity of interfaces between suspensions of different concentrations:

initial suspension (B) and clear liquid (A) is erefore:

maximum flux that the downflow section can take. The critical feed flux is therefore 0.017 mm/s (Solution Manual-Figure 3.12.1). The corresponding feis CFcrit = 0.17. The corresponding concentration in the underflow is found where the critical flux line intersects the underflow flux line (slTto the critUnder critical conditions the flux in the upflow section (CT) is zero and so the overflow concentration CV is zero. Part (b): Referring now to Solution Manual-Figure 3.12.2, if the feed flux concentration is increased to 0.187 (110% of CFcrit), we see that the corresponding feed flux is about 0.0187 mm/s. The thickener is overloaded since the feed concentration is greater than the critical value. The excess flux (0.0187 - 0.017 = 0.0017 mm/s) passes to the upflow section above the feed well. Solution Manual-Figure 3.12.2 shows eoverflow concentratthe feed well is the critical flux, which gives rise to a concentration in this sectCBmin = 0.19 or CBmax = 0.05 and an underflow concentration of CL = 0.34. EXERCISE 3.13: Uniformly sized spheres of diameter 50 μm and density 1500 kg/m3 are uniformly suspended in a liqsu The single particle terminal velocity of the spheres in this0.00034 m/s (Rep < 0.3). Calculate the velocity at which in SOLUTION TO EXERCISE 3.13: (a Text-Equat

The velocity of the interface betweenth

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.23

Uint,AB =UpA AC − UpBCB

CA − CB

Since CA = 0, the equation reduces to Uint,AB = UpB

pB is the hindered settling velocity of particles relative to the vessel wall in batch

o check whether Stokes Law is valid, we calculate the single particle Reynolds

Usettling and is given by Text-Equation 3.24:

nUp = UTε

Tnumber at the terminal velocity:

0085.0002.0

1000104.3)1050( 46

=××××

=−−

Rep

his value is less than the limiting value for Stokes Law (0.3) and so Stokes Law and therefore in Text-Equ tion 3.24 exponent n = 4.65.

he voidage of the initial suspension, εΒ = 1 - CB = 0.70

10-5 m/s

rds.

spheres having a diameter of 155 microns in ater at 293K. The slurry contains 60 wt % solids. The density of the glass spheres

s?

order to calculate the settling velocity o0f the slurry, the single particle settling velocity must first be calculated.

Tapplies a T hence, 65.44

pB 70.0104.3U ××= −

= 6.474 x Hence, the velocity of the interface between the initial suspension and the clear liquid is 0.0647 mm/s. The fact that the velocity is positive indicates that the interface ismoving downwa EXERCISE 3.14: Calculate the settling velocity of glasswis 2467 kg/m3. How does the settling velocity change if the particles have a sphericity of 0.3 and an equivalent diameter of 155 micron SOLUTION TO EXERCISE 3.14: In

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.24

To calculate UT for a given particle size x, calculate the group:

CD Rep2 =

43

x3ρf (ρp2− ρf )g

μ

( )( )

⎥⎥⎦⎢⎣ 001.0

81.93

= 71.4 or spherical particles (ψ = 1.0), Rep = 2

ulated fro :

⎤− 3 ⎢⎡ ×−×××

= 2

6 100024671000)10155(4

Using the standard drag curve (Figure 2.3) fThe terminal velocity UT may be calc m

μρ

== Tvfp

Ux2Re

Hence, terminal velocity, UT = 0.0129 m/s the suspension =

Where n is given by:

Settling velocity of nTp UU ε=

57.0Ar043.04.2nn8.4

=−

−

( )

( )And 5.53001.0

81.9)10002467(100010155g)(xAr 2

6

2fpf =

×−×××=

μ

ρ−ρρ=

−

3

hich gives n = 4.1 slurry is not 0.6. 100 kg of slurry contain 60 kg

f glass spheres and 40 kg water. So the slurry contains 0.0243 m3 glass spheres and 3

3

WNOTE: solids volume fraction of the o0.04 m water. The solids volume fraction of the slurry is therefore 0.38 and ε = 0.62.

the suspension = ( ) 31.4nTp 108.162.00129.0UU −×=×=ε=Settling velocity of m/s

If the particles have a sphericity of 0.3, we need to go back to the standard drag curve for ψ = 0.3. In which case, Rep = 0.3 and so:

alculated from:

The terminal velocity UT may be c

μρ

== Tvfp

Ux3.0Re

ocity, UT = 0.00194 m/s Hence, terminal velSince Rep = 0.3 , n = 4.65 and so: Settling velocity of the suspension = ( ) 4n

T 101.265.462.000194.0 −×=×=εU m/s

kes for a particle settling in a liquid to reach 99% of its terminal velocity.

EXERCISE 3.15: Develop an expression to determine the time it ta

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.25

SOLUTION TO EXERCISE 3.15: Start with the force balance on a single particle:

force drag-forcegravity -forcebuoyancy force onAccelerati =

Thus for a particle in the Stokes region:

( ) uma μπ

ρ= x3g6x

dtdux 3

fp

3

p π−ρ−ρ=π6

CABdu u

Cdt=+ ,

where ( ) g6xA

3

fpπ

ρ−ρ= and 6xC

3

pπ

ρ= , ux3B μπ=

Solve for u: C

BtC

BtC

Bte

CA

CBue

dtdue =+

CBt

CBt

eCA

dt

ued=

⎟⎠⎞

⎜⎝⎛

∫= CBt

CBt

eCAue

1CC Ce

BCue +=

BtBt CA

CBt

1eCAu−

+=C

e initial conditio to find C1:

At t = 0, u = 0. Apply th n

So BAC −= 1

⎟⎠⎞

⎜⎛ −=

−C

Bte1Au Hence,

⎝B

Examining this expressions, we see that as ∞→t , BAu → (terminal velocity).

So we need to know the value of t at which, BA99.0u =

⎟⎠⎞

⎜⎝⎛ −=

−C

Bte1

BA

BA99.0

Solving for t:

( )CBt01.0ln −=

μ

ρ

18x6.4 2

p Gives t =

Therefore, time for a particle to reach 99% of its terminal velocity in the Stokes

region is: t = μ

ρ

18x6.4 2

p

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.26

EXERCISE 3.16: zed spheres (diameter = 150 μm and density =

. The suspension settles to he rate at which the spheres

ttle in the suspension. Calculate the rate at which the settled bed height rises.

a) Solids concentration of initial suspension, CB = 0.25

ion 3.28 allows us to calculate the velocity of interfaces between suspensions of different concentrations:

initial suspension (B) and clear liquid (A) is erefore:

A suspension in water of uniformly-si31140 kg/m ) has a solids concentration of 25% by volume

a bed of solids concentration 62% by volume. Calculate tse SOLUTION TO EXERCISE 3.16: ( Text-Equat

The velocity of the interface betweenth

int,AB =UpA AC − UpBCB

CA − CB U

Since CA = 0, the equation reduces to Uint,AB = UpB

pB is the hindered settling velocity of particles relative to the vessel wall in batch

Assuming first that Stokes Law applies, then:

Usettling and is given by Text-Equation 3.24:

Up = UTεn

( ) ( ) ( ) 001717.0001.01818

U fpT =

×=

μ= 81.91000114010150gx 262 ×−××ρ−ρ −

hecking the Reynolds number, C

2576.0001.0

1000001717.0)10150(xUe6

fT =×××

=ρ

=−

R p μ ion is valid.

re, in Text-Equation 3.24 exponent n = 4.65.

he voidage of the initial suspension, εΒ = 1 - CB = 0.75

506 m/s

Reynolds number is less than 0.3, so Stokes Law assumpt Therefo , T hence, 65.4

pB 75.0001717.0U ×=

= 0.0004

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.27

Hence, the velocity of the interface between the initial suspension and the clear liquid is 0.451 mm/s. The fact that the velocity is positive indicates that the interface is

oving downwards.

gain we apply Text-Equation 3.28 to calculate the velocity of interfaces between suspensions of different concentrations:

he velocity of the interface between initial suspension (B) and sediment (S) is

m (b) Here a

Ttherefore:

Uint,BS =UpBCB − UpSCS

CB − CS

With CB = 0.25 and CS = 0.62 and since the velocity of the sediment, UpS is zero, we have:

pBBSint, U6757.062.025.0

U −=−

=

And fro

pB 025.0U −

m part (a), we know that UpB = 0.451 mm/s, and so

signifies that the interface is moving upwards. So, the interface 5

XERCISE 3.17: f 2000 kg/m3 are suspended in a liquid with a

ntration of 50 kg/m3, what is the solids volume action of the suspension? What is the bulk density of the suspension?

SOLUTION TO EXERCISE 3.17:

50 kg of particles occupies 0.025 m3

mm/s 305.0U BSint, −=

The negative sign between initial suspension and sediment is moving upwards at a velocity of 0.30mm/s. EIf 20 micron particles with a density odensity of 900 kg/m3 at a concefr

Assuming 1 m3 of suspension:

⎟⎟⎠

⎞⎜⎜⎝

⎛3m/kg2000

kg50

025.0volume totalparticles volume

=⎟⎠⎞

⎜⎝⎛ Therefore solids volume fraction =

Bulk density of suspension = ( ) 5.9272000025.0900975.01 pf =×+×=ρε−+ερ kg/m3

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.28

EXERCISE 3.18: Given Figure 3E.18.1 for the height-time curve for the sedimentation of a suspensioin a vertical cylindrical vessel with an initial uniform

n solids concentration of 100

ent/suspension interface rises? uspension of

which a layer of concentration 133 kg/m3 propagates upwards from the base of the vessel?

spension interface start rising? id

SOLUTION TO EXERCISE 3.18: ) At the end of the test we know that the surface of the sediment has risen from

kg/m3. a) What is the velocity at which the sedimb) What is the velocity of the interface between the clear liquid and s

concentration 133 kg/m3? c) What is the velocity at

d) At what time does the sediment/sue) At what time is the concentration of the suspension in contact with the clear liqu

no longer 100 kg/m3?

(ah = 0 to hs = 30 cm in 20 seconds.

Hence the sediment velocity is: s/cm66.12030

+= (upward)

(b) Referring to Solution-Manual-Figure 3.18.1, we must first find the point on the curve corresponding to the point at which a suspension of concentration 133 kg/m3 interfaces with the clear suspension. From Text-Equation 3.38, with C = 133, CB = 100 and h0 = 100 cm, we find:

cm 75133

100100h1 =×

=

A line drawn through the point t = 0, h = h1 tangent to the curve locates the point on

e curve corresponding to the time at which a suspension of concentration 133 kg/m3 ). The coordinates

f this point are

he curve at this point:

thinterfaces with the clear suspension (Solution Manual-Figure 3.18.1ot = 13.5 sec, h = 37.5 cm. The velocity of this interface is the slope of t slope of curve at 13.5 sec, 37.5 cm = s/cm 78.2− downward velocity of interface = 2.78 cm/s

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.29

(c) From the consideration above, after 13.5 seconds the layer of concentration 133 g/m3 has just reached the clear liquid interface and has travelled a distance of 37.5 k

cm from the base of the vessel in this time.

Therefore, upward propagation velocity of this layer = s/cm 78.25.37h+==

5.13t) At time = 0

time curve stops being a straight line. This

thickener of area 300 m2 and a

) What is the concentration of solids in the top section of the thickener? in the bottom section of the thickener?

) What is the concentration of solids exiting the thickener? low the feed?

) What is the flux due to settling below the feed?

.19:

Fro

(d) Flux due to bulk flow = 0.0015 mm/s (from Figure – underflow flux) (d) Continuous total downward flux = 0.01 mm/s Total downward flux = flux due to bulk flow + flux due to settling. Therefore flux due to settling = 0.01 – 0.0015 = 0.0085 mm/s

(d (e) This is the time at which the AB interface disappears. In the figure, this is the time at which the slope of the height versus time is 10 seconds. EXERCISE 3.19: Given Figure 3E19.1 for the fluxes below the feed in afeed solids volume concentration of 0.1, ab) What is the concentration of solidscd) What is the flux due to bulk flow bee SOLUTION TO EXERCISE 3

m Solution Manual-Figure 3.19.1:

(a) CT = 0 for an underloaded thickener (b) CB = 0.04 (from Figure) (c) CL = 0.25 (from Figure)

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.30

Figure 3.E2.1: Batch settling test results. Height versus time curve for use in Exercises 3.2 and 3.4

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.31

Figure 3.E5.1: Batch settling test results. Height versus time curve for use in Exercise 3.5.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.32

Figure 3.E6.1: Batch settling test results. Height versus time curve for use in Exercises 3.6 and 3.8.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.33

Figure 3.E9.1: Batch flux plot for use in Exercise 3.9.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.34

Figure 3.W3.1: Batch flux plot for use in Worked Example 3.3 and Exercise 3.10.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.35

Figure 3.E11.1: Flux plots for use in Exercise 3.11.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.36

Figure 3.2.1: Batch settling test result; solution to Exercise 3.2.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.37

Figure 3.4.1: Batch settling test results; solution to Exercise 3.4.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.38

Figure 3.5.1: Batch settling test results; solution to Exercise 3.5.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.39

Figure 3.6.1: Batch settling test results; solution to Exercise 3.6.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.40

Figure 3.8.1: Batch settling test results; solution to Exercise 3.8.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.41

Figure 3.9.1: Batch flux plot; solution to Exercise 3.9.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.42

Figure 3.9.2: Sketch of concentration profile in batch settling test vessel

after 20 minutes; solution to Exercise 3.9.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.43

Figure 3.10.1: Batch flux plot; solution to Exercise 3.10.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.44

Figure 3.10.2: Sketch of concentration profile in batch settling test vessel after 40 minutes. Solution to Exercise 3.10.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.45

Figure 3.11.1: Batch and continuous flux plots; solution to Exercise 3.11.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.46

Figure 3.12.1: Flux plots and solution for exercise 3.12.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.47

Figure 3.12.2: Flux plots and solution for exercise 3.12 – continued.

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.48

Height(cm)

Time(s)

Figure A

50

100

10 20 30 40

h1 = 75 cm

h = 37.5 cm

t = 13.5 s

slope = -2.78 cm/s

slope = +2.78 cm/s

slope = +1.66 cm/s

Figure: Solution Manual-Figure 3.18.1

Height(cm)

Time(s)

Figure A

50

100

10 20 30 40

h1 = 75 cm

h = 37.5 cm

t = 13.5 s

slope = -2.78 cm/s

slope = +2.78 cm/s

slope = +1.66 cm/s

Figure: Solution Manual-Figure 3.18.1

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.49

0.01

0.02

0.03

mms

PSU

⎛ ⎞⎜ ⎟⎝ ⎠

0.1 0.2 0.3 0.4 C

Feed Flux

Downward Flux Below Feed

Underflow Flux

Figure B

CLCFCB

0.0015 mm/s

Solution Manual-Figure 3.19.1 – Solution to Exercise 3.19

0.01

0.02

0.03

mms

PSU

⎛ ⎞⎜ ⎟⎝ ⎠

0.1 0.2 0.3 0.4 C

Feed Flux

Downward Flux Below Feed

Underflow Flux

Figure B

CLCFCB

0.0015 mm/s

0.01

0.02

0.03

mms

PSU

⎛ ⎞⎜ ⎟⎝ ⎠

0.1 0.2 0.3 0.4 C

Feed Flux

Downward Flux Below Feed

Underflow Flux

Figure B

CLCFCB

0.0015 mm/s

Solution Manual-Figure 3.19.1 – Solution to Exercise 3.19

SOLUTIONS TO CHAPTER 3 EXERCISES: MULTIPLE PARTICLE SYSTEMS Page 3.50