PART 3 - Transport Phenomena in Bioprocess System Flashcards

Determination and Factors Affecting KLa values - Degree of Agitation - Medium Culture Rheology

1
Q

According to _____________________________ (1961), two correlations adequately explain their data regarding the absorption of gases that are sparingly soluble into liquids that subsequently chemically consume the gas.

A

Calderbank and Moo-Young

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2
Q

There are two clear regimes of bubble-swarm mass-transfer, with a critical bubble diameter Dc indicating the boundary between them. Dc ≈ 2.5 mm when surfactants are not present:

A

Bigger bubbles
Smaller bubbles

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3
Q

_________ bubbles than this are usually found in sieve-plate columns and agitated tanks containing pure water.

A

Bigger

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4
Q

__________ bubbles are commonly observed in agitated vessels containing hydrophilic solutes in aqueous solution and sintered-plate columns.

A

Smaller

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5
Q

What are the factors affecting bubble size?

A
  1. Bubble formation
  2. Bubble breakup
  3. Bubble coalescence
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6
Q

It is determined by instabilities in the gas stream that enters the liquid phase, which cause the stream to fragment into separate bubbles instead of moving continuously through the vessel.

A

Bubble formation

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7
Q

It depends on the competition between surface tension, which stabilizes the bubble, and local fluid forces, which tend to tear the bubble apart.

A

Bubble breakup

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8
Q

The probability of _______________________ depends on the properties of the gas-liquid interface.

A

bubble coalescence

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9
Q

In real dispersions, like those involving bubbles in a liquid, often encounter a variety of bubble sizes rather than a uniform size throughout. This variation is known as a:

A

distribution of bubble sizes

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10
Q

To characterize this distribution and provide a representative size, the ________________________________________ is utilized.

This is a surface-averaged measurement, offering a characteristic or mean size for the bubbles present in the dispersion.

A

Sauter mean bubble diameter (Dsm)

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11
Q

___________ (1983) reviewed a number of studies on gas-liquid mass transfer in low viscosity fluids in agitated vessels.

The relationship fits the results of numerous experiments conducted in various vessels with various mixer configurations within a 20–40% range.

A

Van’t Riet

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12
Q

What are the factors affecting KLa values in bioreactor ?

A
  1. Estimation of Diffusivities
  2. Ionic Strength
  3. Surface-Active Agents
  4. Effects of Electrolytes
  5. Presence of Cells
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13
Q

The __________________________________ is frequently used to compare the effectiveness of bioreactors and as an important scale-up factor.

A

volumetric mass transfer coefficient (kLa)

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14
Q

______________ can be referred to as the measurement of the total concentration of ions in the solution, weighted by ion charge. It is denoted by 𝜇.

The greater the magnitude of the charge, the ________ the magnitude of the concentration, and thus the __________ the ionic strength.

A

Ionic strength

greater
greater

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15
Q

Many biochemicals are ____________, meaning they contain hydrophilic and hydrophobic moieties that tend to concentrate at gas-liquid and liquid-liquid interfaces.

A

amphipathic

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16
Q

What is a moiety?

A

A moiety is a part of the chemical structure of a molecule or compound that could include a substructure, such as a functional group.

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17
Q

Most of kLa data published are gathered through physical absorption or desorption using clean water.

It is common knowledge that mechanical force-generated bubbles in electrolyte solutions are considerably _______ than those in pure water.

A

smaller

18
Q

The physical presence per se of microbial cells in the broth will affect the kLa values in ___________________________.

A

bubbling-type fermenters.

19
Q

The rates of oxygen absorption into aqueous suspensions of sterilized yeast cells were measured in:

A

(i) an unaerated stirred tank with a known free gas–liquid interfacial area.
(ii) a bubble column; and
(iii) an aerated stirred tank.

20
Q

Data acquired with scheme (i) showed that the kL values were only minimally affected by the presence of cells, whereas for schemes (ii) and (iii), the gas holdup and kLa values were decreased somewhat with increasing cell concentrations, due to increased bubble sizes.

A
21
Q

_______________ the fermentation broth ensures uniform air distribution within the medium. When you blend a solution, you introduce energy into the system.

A

Agitating

22
Q

Higher power input leads to ________ bubbles, thereby increasing the interfacial area. Consequently, the mass transfer coefficient is expected to be influenced by both the power input per unit volume of the fermentation broth and the gas’s superficial velocity.

A

smaller

23
Q

The discussion of agitation that follows pertains to fluids that exhibit characteristics similar to Newtonian fluids.

A
24
Q

Since mixing is a multifaceted process, the relevant factors are collectively evaluated using a dimensionless parameter called the ______________. This number is employed to describe the flow behavior.

A

Reynolds number (Re)

25
Q

Another set of dimensionless parameters employed to describe mixing in a container is the ________________, which incorporates gravitational forces into its calculation:

A

Froude number (Fr)

26
Q

_____________________ is influenced by fluid properties, including fluid density and viscosity, the agitator’s rotational speed, and the impeller’s diameter.

A

Power consumption

27
Q

Four Types of Agitators:

A
  1. Turbine Disk (Rushton)
  2. Turbine Inclined Blades
  3. Propeller, marine type
  4. Intermig
28
Q

To achieve optimal mixing, a turbine typically features between four to six blades. Turbines equipped with flat blades create a radial flow pattern, which proves effective for dispersing gas within the medium. In this process, the gas is introduced just beneath the impeller, drawn upward to the blades, and fragmented into consistent, small bubbles.

A

A. Turbine disk (Rushton)

29
Q

The most common type of agitator is turbine. It consists of several short blades mounted on a central shaft. The diameter of a turbine is normally 35–45% of the tank diameter.

A

B. Turbine inclined blades

30
Q

The propeller agitator with three blades rotates at relatively high speeds of 60–300 rps; highly efficient mixing is obtained. The generated flow pattern is axial flow since the fluid moves axially down to the center and up the side of the tank.

A

C. Propeller, marine type

31
Q

The intermig agitator represents a relatively new innovation in agitator design. It takes the form of an axial pumping impeller with blades positioned at opposing angles to each other. Comparing an intermig agitator to a disk turbine agitator, the former delivers a more uniform energy transfer to the liquid in the container. As a result, this agitator requires lower power and less air input to achieve equivalent mixing and the same mass transfer coefficient.

A

D. Intermig

32
Q

__________ is the science of deformation and flow. It is the study of how matter flows, often in a liquid state, but also in the case of “soft solids” or solids that deform under a specific force rather than bouncing back elastically

A

Rheology

33
Q

This fluid can be identifiable by a single viscosity coefficient at a particular temperature.

In this case, viscosity varies with temperature but remains constant with respect to strain rate.

A

Newtonian Fluid

33
Q

This is a wide range of fluids whose viscosity is influenced by strain rate (the relative flow velocity).

The categorization of these fluids is determined by how shear stress and shear rate are connected within the fluid.

A

Non-Newtonian Fluid

34
Q

This denotes how a material’s deformation or strain changes over time.

A

Strain rate

35
Q

All gases, water, dispersions of gas in water, low-molecular-weight liquids, aqueous solutions of low-molecular-weight

A

Newtonian

36
Q

Rubber solutions, adhesives, polymer solutions, some greases, starch suspensions, cellulose acetate, mayonnaise, some soap and detergent slurries, some paper pulps, paints, wallpaper paste, biological fluids

A

Pseudoplastic

37
Q

Cornstarch-water mixture, quicksand

A

Dilatant

38
Q

Some plastic melts, margarine, cooking fats, some greases, toothpaste, some soap and detergent slurries, some paper pulps.

A

Bingham Plastic

39
Q

Blood, tomato sauce, orange juice, melted chocolate, printing ink

A

Casson Plastic

40
Q
A
41
Q
A