Exam 3 Flashcards

(61 cards)

1
Q

Which of the following regular polyghedrons is most likely to have the highest sphericity? Why?

Tetrehedron
Dodecahedron
Cube
Octahedron

A

Dodecahedron

Since it has the most faces (12), in has the most symmetry making it closest in resemblance to a sphere

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2
Q

What does bed voidage describe?

A

The fraction of a packed bed’s volume not taken up by particles

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3
Q

Do the friction losses increase, decrease, or stay the same if a packed bed becomes more densely packed? Why?

A

Increase

This is because when packing density increases, the bed becomes more resistant to fluid flow due to reduced void space and increased surface area for interaction, causing the frictional losses to increase

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4
Q

Does the superficial velocity increase, decrease, or stay the same if a packed bed becomes more densely packed ?

A

Increases

As the bed becomes more densely packed, the volume of void space between the particles decreases since the same flow rate is passing through a smaller total cross-sectional area ( due to its reduced void space ) , the fluid must move faster through the remaining available space . u= V/A

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5
Q

If the diameter of particles in a packed bed increases, do the frictional loses increase , decrease, or stay the same? Why?

A

Decrease

Larger particles result in less resistance to flow, and this leads to a decrease in frictional losses.

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6
Q

When the Reynolds’s number is large in a packed bed, what role do viscous forces/ effects play?

A

Viscous effects are unimportant so there is little energy dissipation through friction

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7
Q

How does the superficial velocity compare to the actual velocity in a packed bed for a given flow rate?

A

It’s smaller

Why?
The packing causes the fluid to have less space to flow through so its velocity is higher with packing .

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8
Q

Increasing the mesh number of a screen allows:

A

Larger particles to be blocked
Fewer particles to pass through

Why? Increasing the mesh number makes the screen finer

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9
Q

Is the potential energy term in a mechanical energy balances negligible in liquids or gases? Why?

A

Gases

Changes in potential energy are typically small due to the low density of gases

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10
Q

When the Reynolds’s number for a packed bed is greater than 1000, what term is negligible?

A

Viscous

For high Reynolds’s number (Re> 1000), the flow is dominated by inertial forces (turbulence), and the impact of viscous forces becomes less important making the viscous term negligible

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11
Q

True or False?
Because frictional loses are so high In packed beds, we will often ignore frictional loses in other places in the pipe

A

True

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12
Q

The fluid velocity equals Umf in a bed. What would happen to the bed if all other conditions remain the same , but the cross-sectional area of the bed decreases?

A

The bed becomes packed and is no longer fluidized

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13
Q

Consider a packed bed through which you can flow either water or air. If you increase the superficial velocity over the minimum velocity by some constant value, how would you expect it to change the bed length in each case?

A

The bed would be larger when water is flowed then when air is flowed

Why?
Water has a higher density and viscosity which will require a longer bed length to achieve the same fluidization because the increase in superficial velocity has a less significant effect on fluidization in the packed bed

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14
Q

For a fluidized bed, if the superficial velocity increases to above the terminal velocity, what happens?

A

Particles begin being ejected from the bed
The frictional pressure drop decreases

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15
Q

List the steps to solve for the diameter of a particle (dp)

A
  1. Calculate the volume of the shape.
  2. Set the volume of the sphere equal to the shapes volume.
  3. Calculate the diameter of the sphere.
  4. Calculate the surface area of the sphere for that same volume.
  5. Calculate the surface area of the shape.
  6. Divide the surface area of the sphere by the surface area of the shape to get sphericity
  7. Multiply the diameter of the sphere by the sphericity.
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16
Q

List the steps to solve for the sphericity of a particle

A
  1. Calculate the volume of the shape.
  2. Set the volume of the sphere equal to the shapes volume
  3. Calculate the radius of the sphere.
  4. Calculate the surface area of the shape.
  5. Calculate the surface area of the sphere.
  6. Divide the surface area of the sphere by the surface area of the shape.
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17
Q

What is a packed Bed? Give some examples

A

A packed bed refers to a type of column or reactor where solid particles are packed into a container or tube, leaving empty space (or voids) between the particles.
Examples: rock piles, sand filters, soil in flower pots, cigarettes, and absorption columns

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18
Q

What is the equation for sphericity?

A

The surface of sphere over the surface of the particle at the same volume

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19
Q

What is the sphericity of a sphere?

A

1

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20
Q

What is dsph? How is it different from dp? How do you calculate dp using dsph?

A

dsph is defined as the equivalent spherical diameter. It can be calculated by (6V/pi)^1/3 using the same volume as the particle. Dp is the diameter of the actual particle. dp is equal to dsph times sphericity.

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21
Q

Does the voidage increase or decrease as the sphericity decreases for randomly packed beds of uniform particles?

A

The voidage increases

Non spherical particles tend to pack less efficiently, leading to more gaps or voids between the particles

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22
Q

For chapter 6 equations for Frictional loss for packed Beds, what density is used?

A

The density of the fluid

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23
Q

What is superficial velocity and how does it relate to regular velocity?

A

Superficial Velocity (u0) is a term used to describe the flow rate of a fluid through a packed bed , assuming that the fluid is moving through the entire cross- sectional area of the bed (as if there were no solid particles).

Regular velocity (u) is the actual velocity of the fluid while it moves through the packed bed. u = u0 /E (porosity)

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24
Q

Are the frictional losses much greater or much smaller in the packed bed section compared to the rest of the pipe?

A

The frictional losses are much greater in the packed bed section.

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25
When is this condition satisfied? When the density of the fluid does not vary much as it passes through the packed bed, one can use the average fluid density in the system. Thus, change in pressure/ the average density
This condition is satisfied for all liquids and for gases where the relative variation is less than 10% The change in pressure < 0.1 (Average Density)
26
Describe The Fluidized State
As we progressively increase the velocity of fluid which is flowing upward through a batch of solids. The frictional resistance increases, and eventually a point is reached were the resistance just equals the weight of the solids. At this point the solids become suspended , aka fluidized.
27
What is umf?
The velocity of fluid needed to just fluidize the solids is called the minimum fluidizing velocity (umf).
28
What are the variables of E, L, and U for a Fixed bed?
Em, Lm, u0< umf
29
What are the variables for L,E, and U for minimum fluidization?
Lmf, Emf, and u0=umf
30
What are the variables of L,E, and u for Smooth Fluidization ( Liquids ) ? What is the relationship between Lmf and u0?
Lf,Ef, and u0 > umf With Liquids the bed expands more and more as u0 rises
31
What are the variables of L,E, and u for Liquid Fluidization ( Gases ) ? What is the relationship between Lmf and u0?
Lf,Ef, u0> umf With gases the bubbles are seen and the bed level changes little as u0 rises.
32
The Force causing particle to accelerate = net weight of particle - (what?)
The drag force
33
What is Cd?
Cd is the drag coefficient
34
Define terminal velocity
A constant speed that a freely falling object eventually reaches when the force of gravity pulling it downward is balanced by the drag force (air resistance) acting upward
35
How does the mass of an object affect its terminal velocity?
A heavier object experiences a greater gravitational force, which means it will require more drag to balance the forces, leading to a higher terminal velocity
36
How does the shape and size of the object affect the Terminal Velocity?
Objects with larger surface areas experience more drag, which slows them down. More streamline (aerodynamic) shapes generally experience lower drag and have higher terminal velocities.
37
How does the density of the fluid affect the terminal velocity?
In denser fluids (like water or air at higher altitudes), drag is greater, so terminal velocity is lower
38
How does Cd ( the drag coefficient ) affect the terminal velocity?
The drag coefficient is a dimensionless number that characterizes the drag force acting on an object. It depends on the shape, texture, and orientation of the object.
39
What is the volume of a cube with length, width, and height a?
V = a^3
40
What is the volume of a rectangle with length = l, height = h, and width = w?
V = l*w*h
41
What is the volume of a cone?
V = 1/3*pi*r^2*h
42
What is the volume of a cylinder?
V = pi*r^2*h
43
What is the volume of a sphere?
V = 4/3 * pi * r^3
44
What is the surface area of a cube with l,w,h = a?
SA = 6a^2
45
What is the surface area of a rectangular prism using variables l, w, h?
SA = 2(wl + hl+ hw)
46
What is the surface area of a cone?
SA = pi * r ( r + sqrt(h^2 + r^2)
47
What is the surface area of a cylinder?
SA = 2*pi*r*h + 2*pi*r^2
48
What is the surface area of a sphere?
SA = 4*pi*r^2
49
True or false? The change of kinetic energy is important in packed beds because velocities generally drop across them .
False
50
How do you calculate bed voidage?
(The volume of the bed - the volume of the packing) / (the volume of the bed)
51
In equations for packed beds, what velocity is used, superficial or real? Why?
Superficial velocity. This is because we could never estimate or calculate the real velocity because packing materials may be uneven.
52
When calculating friction losses for a packed bed using the Ergun equation, which L is used?
The length of the packed bed
53
What two phases can flow through packed beds? What direction will they each flow?
Liquids and gases. Gases, flow upward and liquids flow down to avoid needing pumps/compressors, we take advantage of nature and columns are vertical.
54
If the phase flowing through the packed bed is a gas, what formula do we use to calculate the density?
Density = ( MW * P) / (R * T)
55
If the packed bed length is not very long, will the pressure drop through the bed be big or small?
Small
56
True or false? Once the fluidization velocity is reached, the pressure drop across the bed becomes constant?
True
57
For fluidized beds, when would the flow go up?
If the particles are denser than the fluid.
58
For fluidized beds, when would the flow go down?
When the particles are less dense than the fluid.
59
For a fluidized bed with liquid flowing through, will Lmf be less than, equal to, or greater than Lf? If not equal than. Will it be greater or less than by a lot or a little?
Lmf will be a lot less than Lf
60
For a fluidized bed with gas flowing through, is Lmf less than or greater than Lf? By a lot or a little?
Lmf is a little less than Lf
61
What is archimedes number (AR) ? What does a higher AR mean?
It is a dimensionless number that can describe the motion of fluids due to density differences. This gives information on how easily particles can be fluidized. A higher AR means that gravitational forces are higher than viscous forces, and the particles are more likely to settle and require a higher velocity to achieve fluidization