Drying Flashcards

1
Q

Why is drying performed?

A
  • Prevents chemical degradation, physical aggregation or precipitation
  • Aids in formulation (can remove volatile contaminants)
  • Helps with storage (biological products are thermally labile so cannot use high T)
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2
Q

2 forms of water in biological solids:

A

Unbound water:

  • Water in equilibrium with vapour phase (same vapour pressur)
  • Held mainly in voids of the solid

Bound water:

  • In fine capillaries
  • Very low vapour pressure
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3
Q

Dry Basis vs Wet Basis

A

Dry:
x_a = m_a/m_b

Wet:
w_a = m_a/m_t
=m_a/(m_a + m_b)

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4
Q

Define Relative Saturation

A

Phi = p_i/p_i*

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5
Q

Define Humidity

A

Mass of H2O per mass of dry air:

H = m_w/m_a = M_wp_w/(M_a(P-p_w))

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6
Q

Relationship between concentration and humidity

A

c_w = p_w/RT

c_w = H(M_a/M_w)/(1+H(M_a/M_w))*P/RT

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7
Q

Relative Saturation

A

Phi = (pw/pw*) * 100

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8
Q

Describe the two drying periods

A

Constant Drying Period
- r.d.s: removal of liquid from surface to bulk

Falling Drying Period
- r.d.s: internal diffusion of water to cake surface

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9
Q

Describe the two falling drying periods

A

First falling period

  • wet surface
  • r.d.s: transfer of moisture to surface

Second falling period

  • dry surface: plane of separation in the solid
  • r.d.s: molecular diffusion through solid (largely independent of conditions outside solid)
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10
Q

Define Hygroscopic

A

Strong interaction with water

No constant drying period

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11
Q

Constant drying period equation and assumptions

A

w = k_gA(p_s - p_w)

Assumes drying takes place from a saturated surface

In case of wind:
w = k_gA(p_s - p_w)*u^0.8

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12
Q

Heat transfer equations required for vacuum shelf dryer with moving wet solid level

A

Heat Transfer:
q = k(T_0 - Ts)/y

Heat in = Heat to vaporise water:
qA = -LambdaroA(dy/dt)

  • Insert for q
  • Integrate and solve (y=d at t=0)
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13
Q

Falling rate period: drying mechanism

A

Diffusion Theory: Movement of water is governed by diffusion (Fick’s Law)

Capillary Theory: Movement of water due to Capillary forces

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14
Q

Sherwood and Newman solution to Fick’s Law

A

Truncated to only the first term for long drying times (Dt/d^2 > 0.1):

-dXm/dt = (pi^2 D)/(4d^2) *(Xm - Xe)

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15
Q

Constant dying period empirical equation

A

Assume rate of dring is proportional to free moisture content:

Rc = -1/A *dX/dt

tc = (X1 - Xc)/(A*Rc)

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16
Q

Falling rate drying period

A

dX/dt = -mA (X - Xe)

tf = 1/(m*A) *ln((Xc - Xe)/(X - Xe))

17
Q

Solving for Total drying time

A

Falling and constant drying rates are the same at Xc

Rc = mA(Xc -Xe)

18
Q

Means of heat supply in drying processes

A
  • Direct heat transfer (hot gas)

- Indirect heat transfer (heat exchange surface, microwave, radiative)

19
Q

Means of vapour removal in drying processes

A
  • Cross flow of carrier gas
  • through flow of carrier gas
  • suction
20
Q

Means of solid motion in drying processes

A
  • Static (fluidised bed) vs agitated (e.g. tumble drum or agitated vessel)
21
Q

Freeze Drying process description

A
  • Decrease T below triple point Temp to freeze moisture
  • Decrease P to below triple point pressure
    (First 2 steps on the order of hours)
  • Increase T & decrease P to cause sublimation (primary drying of unbound liquid)
  • Further increase of T and decrease P (secondary drying of bound liquid)
    (time of these steps on the order of days)
22
Q

When is freeze drying used

A

Thermally labile proteins or hygroscopic solids