PART 1 - Transport Phenomena in Bioprocess System Flashcards

Gas-Liquid Mass Transfer in Cellular Systems

1
Q

Mass can be transferred from one place to another under the influence of a__________________________ or____________________ in the system.

A

concentration difference
concentration gradient

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2
Q

A simple example is when dye is dropped into a cup of water, mass-transfer processes are responsible for the movement of dye molecules through the water until _____________ is established and the concentration is __________.

A

equilibrium
uniform

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3
Q

In biological multiphase systems, mass transfer takes place between ___________________, between a liquid and a solid phase, or between a gas and a liquid phase.

A

two liquid phases

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4
Q

Most large-scale ____________________ (excluding ______________________ production) are aerobic and typically conducted in aerated gas-liquid bioreactors.

A

fermentation processes
bioethanol and lactic acid

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5
Q

Before being utilized, oxygen must be moved via a sequence of processes from the _________ onto the _________ of cells. The solubility of oxygen within broth is typically very _______.

As a result, during aerobic cultures and fermentations, improving gas-liquid mass transfer is always given priority.

A

gas bulk
surfaces

low

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6
Q

When sparingly soluble oxygen gas is transferred from a source, such as a rising air bubble, into a liquid phase that contains cells or liquid hydrocarbons used in hydrocarbon fermentation, it must pass through a ________________________________.

This refers to the relative magnitudes of which are determined by bubble (droplet) hydrodynamics, temperature, cellular activity and density, solution composition, interfacial phenomena, and other variables.

A

series of transport resistances

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7
Q

Enumerate the transport resistances while explaining the transport process of oxygen from a gas bubble to inside a cell.

A
  1. Diffusion from bulk gas-liquid interface.
  2. Movement through the gas-liquid interface.
  3. Diffusion of the solute through the relatively unmixed liquid region adjacent to the bubble
    into the well-mixed bulk liquid.
  4. Transport of the solute through the bulk liquid to a second relatively unmixed liquid region
    surrounding the cells.
  5. Transport through the second unmixed liquid region associated with the cells.
  6. Diffusive transport into the cellular floc, mycelia, or soil particle.
  7. Transport across the cell envelope and two intracellular reaction sites (e.g. the mitochondria)
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8
Q

When the organisms take the form of individual cells, the _______ resistance disappears.

A

sixth

  1. Diffusive transport into the cellular floc, mycelia, or soil particle.
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9
Q

Microbial cells themselves have some tendency to _____________________. Thus, cells may preferentially gather at the vicinity of the gas-bubble-liquid interface.

A

adsorb at interfaces

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10
Q

Adsorption of microbes/cells at interfaces!

Then, the diffusing solute oxygen passes through only _______________________________ before reaching the cell.

In this situation, the bulk dissolved O2 concentration does not represent the __________________ for the respiring microbes.

A

one unmixed liquid region and no bulk liquid

oxygen supply

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11
Q

_____________________ on or near the hydrocarbon-emulsion interface has also been observed in the microbial utilization of other sparingly soluble substrates such as hydrocarbon droplets.

A

Cell adsorption

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12
Q

In general, we can distinguish fluid motions induced by: (2)

A
  • freely rising or falling bubbles or
  • particles from fluid motion that occur as the result of applied forces other than the external gravity field (forced convection).
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13
Q

Gas-liquid mixing and slowly stirred semi-batch system may have ________ contributions from naturally convected levels and mechanical stirring.

A

equal

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14
Q

Gas-liquid contacting modes via free-falling, falling particles, fluids: (7)

A
  1. Rising single bubble
  2. Bubble swarms
  3. Staged counter-current fermentor
  4. Sparged airlift
  5. Trickle filter counter current
  6. Stratified, nearly horizontal flow
  7. Naturally turbulent aeration
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15
Q

Gas-liquid contacting modes via mechanically agitated: (5)

A
  1. Semi-batch (batch liquid, continuous air
  2. Continuous liquid and air
  3. Multiple propellers (semi-batch or continuous)
  4. Stirred tank with baffles (baffles are often used in designs 1 and 2 also)
  5. Staged cross-current
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16
Q

What do you mean by sparged?

A

moisten by sprinkling with water, especially in brewing.

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17
Q

What do you mean by trickle?

A

flow in a small stream

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18
Q

What do you mean by stratified?

A

placed close together in layers

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19
Q

Mass transfer takes place by two basic processes: (2)

A
  1. Convection
  2. Diffusion
20
Q

_______________________ is the movement of component molecules in a mixture under the influence of a concentration difference in the system.

A

Molecular diffusion

21
Q

Diffusion of molecules occurs in the direction required to ____________ the concentration gradient.

A

eliminate

  • to be in equilibrium
22
Q

If the gradient is maintained by constantly supplying material to the region of high concentration and removing it from the region of low concentration, diffusion will be _______________. This situation is often exploited in mass-transfer operations and bioreaction systems.

A

continuous

23
Q

It states that the molar flux of component A relative to the average molal velocity of all
constituent JA is proportional to the concentration gradient dCA/dz as expressed in:

A

Fick’s First Law of Diffusion

24
Q

What is DAB

A

Diffusivity of Component A through B

25
Q

This is a measure of diffusive mobility

A

Diffusivity

26
Q

The molar flux relative to stationary coordinate NA is equal to:

A

NA = Ca/C (Na-Nb)…..

27
Q

The kinetic theory of liquids is much less advanced than that of gases. Therefore, the correlation for diffusivities in liquids is _________________ as that for gases

A

not as reliable

28
Q

This correlation is the most widely used for dilute solutions of nonelectrolytes.

A

Wilke-Chang correlation (Wilke and Chang, 1955)

29
Q

When the solvent is ________, ________ (1974) recommends the use of the correlation developed by ___________________

A

water

Skelland
Othmer and Thakar

30
Q

This theory states that two fictitious films are present on either side of the interface that cause the overall resistance to mass transfer and that takes place due to molecular diffusion.

A

Two-Film Theory

31
Q

Two-Film Theory

______________________ are assumed to exist only in the films.

Outside the film, the phases are assumed to be at _______________________ and are referred to as gas bulk and liquid bulk.

A

Concentration gradients
uniform concentrations

32
Q

Mathematically, the two-film theory states that kl (mass-transfer coefficient) varies _________ as the film thickness δ, whereas kl and DAB (diffusivity) are ________ proportional to each other.

A

inversely
directly

33
Q

The _____________________ assumes that turbulent eddies travel from the bulk to the interface and at the interface, they remain for an exposure time equal to ____.

A

penetration theory

t0

34
Q

___________ came up with the penetration theory in 1935

A

Higbie

35
Q

In addition, the process of unsteady-state molecular diffusion is assumed in this theory by which the solute is assumed to:

A

Penetration theory

penetrate a given eddy during its stay at the interface

36
Q

This theory assumes that there is a region in which steady-state molecular transfer is controlling

A

film

36
Q

This theory assumes that the interface is continuously replaced by eddies and that unsteady state molecular transfer into the eddies controls the transfer in this region.

A

Penetration theory

36
Q

In contrast to the two-film theory, the penetration theory predicts that kl (mass-transfer coefficient) and the square root of DAB (molecular diffusivity) are ________ proportional, whereas kl varies __________ as the exposure
time t0
.

A

directly
inversely

36
Q

In 1951, ___________ modified Higbie’s penetration theory for liquid phase mass transfer.
The modified theory is widely known as the _______________________.

A

Danckwerts
Surface renewal theory

37
Q

What does the surface renewal theory state?

A

The surface renewal theory
states that a portion of the mass-transfer surface is replaced with a new surface by the motion of
eddies near the surface assuming that the liquid elements at the interface are randomly
swapped by fresh elements from bulk and each of the liquid elements at the surface has the same probability of being substituted by a fresh element.

38
Q

Similar to the penetration theory, the mass transfer coefficient in surface renewal theory is ________ proportional to the square root of diffusivity.

A

directly

39
Q

For sparingly soluble species such as oxygen or hydrocarbons in water, the two equilibrated interfacial concentrations cgi and cli on the gas and liquid sides, respectively, may typically be related through a _________________________ such as ________ law.

A

linear partition-law relationship
Henry’s la

40
Q

The oxygen-transfer rate per unit of reactor volume QO2 is given by:

A

(flux)(interfacial area)/reactor liquid volume

41
Q

The maximum possible utilization is:

A

xmyumax/Yo2

42
Q

Oxygen may also be consumed as a reactant in __________________________.

A

biotransformation

43
Q
A
44
Q
A