Filtration Flashcards

1
Q

Darcy’s Law

A

u_c = K(-dP)/l

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2
Q

Define Permeability constant

A

K = B/mu

Where B = permeability constant
So:
u_c = B(-dP)/(mu*l)

Purely a function of the cake

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3
Q

Specific surface area

A

S = A/V

e.g for a sphere S = 6/d

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4
Q

Specific bed area

A

Surface area presented to the fluid per volume of the bed

S_B = A/V_bed
= A/(V_p/(1-eps))
= A(1-eps)/V_p

V_p = Volume occupied by particles

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5
Q

Carman-Kozeny Equation Theory

A

Assumes free space in powder bed consists of a series of tortuous channels
Assumes cake is uniform
Assumes voidage is constant (unlikely)

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6
Q

Carman-Kozeny Equation Derivation

A

Start with:
u1 = dm’^2 (-dP)/(K’mu*l’)

  • dm’ = eps/S_b
    = eps/(S*(1-eps))
  • u1 = u_c/eps
  • K’l’ = K’‘l

Insert those terms into equation and arrange for u_c

Insert K’’ = 5 (unless different)
Insert S = 6/d for a sphere

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7
Q

What do the u_c, u1, dm’, and l’ terms mean in the Carman- Kozeny derivation

A

u_c = mean velocity over entire tube (Q/A)

u1 = mean velocity through tubes (Q/(eps*A))

dm’ = equivalent diameter of pore

l’ = channel length

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8
Q

Give the equation for the permeability B from the Carman-Kozeny equation and Darcy’s Theory

A

B = eps^3 /(K’’ *S^2 * (1-eps)^2)

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9
Q

Carman plot equation

A

R/(rou^2) = 5Re^-1 + 0.4*Re^-0.1

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10
Q

Equation for the effect Tortuosity has on K’’

A

K’’ = (l’/l)^2 * K_0

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11
Q

Equation for the correction factor due to the wall effect on K’’

A

fw = (1 + Sc/(2*S))^2

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12
Q

Factors affecting K’’

A
  • Tortuosity
  • Wall effects (particles not packed as closely at the walls so resistance is not as great. Deviation is greater for smaller pipe diameters)
  • Mixed sizes of particles such as filter aids can reduce packing & increase channel diameter
  • High voidage(usually for non-spherical particels e.g. fibres/rings)
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13
Q

Factors affecting the rate of filtration

A
  • Pressure drop
  • Filtering surface area
  • Viscosity of filtrate
  • Resistance of filter cake
  • Resistance of filter medium
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14
Q

What stage of cake formation is most important?

A

Initial phase:

  • Rate of flow is greatest at the beginning (minimum resistance)
  • High Initial rates may result in plugged pres (results in higher resistance)
  • Orientation of particles in initial layer
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15
Q

Incompressible cake equation

A

uc = 1/A dV/dt = (-dP)/(rmu*l)

r = 1/B
= specific resistance

r is taken to be constant

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16
Q

Compressible cakes

A

1/A dV/dt = 1/(rmu) *(-dP/dz)

r = f(eps)
eps = f(z)

dV/dt = A^2/(muv’r) *(-dP/dV)

17
Q

Pretreatment of slurries before filtration

A
  • Dilute solution

- Add filter aids