PART 4 Flashcards

1
Q

IMMOBILIZED CELL SYSTEMS

A

High cell concentrations
Cell reuse
Eliminates cell washout at high dilution rates
High volumetric productivities
May provide favorable microenvironment
Genetic stability
Protection from shear damage

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2
Q

MAJOR LIMITATION

A

Mass transfer (diffusional) resistance

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3
Q

ADVANTAGE OVER IMMOBILIZED ENZYMES

A

Whole cells provide cofactors, reducing power, energy that many enzymatic reactions require.

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4
Q

Types of Immbolization

A

Active Immbolization and Passive Immbolization

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5
Q

______________: similar to enzyme
immobilization. Entrapment and binding.

A

Active Immobilization

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6
Q

______________: Biofilm multilayer growth
on solid surfaces.

A

Passive Immobilization

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7
Q

Most widely used method of cell immobilization

A

Physical Entrapment

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8
Q

Various matrices

A

porous polymers (agar, alginate, carrageenan, polyacrylamide, chitosan, gelatin, collagen)

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9
Q

Physical Entrapment

A
  • Porous metal screens
  • Polyurethane
  • Polystyrene
  • Silica gel
  • Cellulose triacetate
  • Polymer Beads are also typically used
  • Encapsulation
  • Macroscopic membrane-based reactors (hollow fiber)
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10
Q

Methods of preparing polymer beads:

A
  • Gelation of polymers
  • Precipitation of polymers
  • Ion exchange gelation
  • Polycondensation
  • Polymerization
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11
Q
  • There is direct contact between nutrient and support materials
  • High cell loadings
  • Disadvantage: porous support materials causes intraparticle pore diffusion (at high cell densities) and hard to control microenvironmental conditions
  • Selection of suitable support materials is highly based on adsorption capacity and strength of binding
A

Physical Adsorption

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12
Q

Widely used for enzymes but not for cells

In general, good support materials should be rigid and chemically inert, should bind cells firmly, high loading capacity

A

Covalent Binding

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13
Q
  • Multilayer growth of cells on solid support surfaces
  • Support materials can be biologically active or inert
  • Common in waste water treatment and mold fermentations
A

Passive Immobilization: Biological Films

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14
Q

Diffusional Limitations

A
  • Analysis similar to immobilized enzymes
  • Damkohler number
  • Effectiveness factor
  • Thiele modulus
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15
Q

Immobilized-Bioreactors

A
  • Packed-column
  • Fluidized-bed
  • Airlift
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16
Q

_____________: feed flows through a column packed with immobilized cells. Similar to a plug flow reactor. Can be recycle chamber.

A

Packed-column

17
Q

_____________: feed flows up through a bed of immobilized cells, fluidizing the immobilized cell particles.

A

Fluidized-bed

18
Q

_____________: air bubbles suspend the immobilized cell particles in a reactor.

19
Q

Solid-state Fermentations

A
  • Fermentations of solid materials
  • Low moisture levels or water activities
  • Agricultural products or foods
  • Smaller reactor volume
  • Low contamination due to low moisture
  • Easy product separation
  • Energy efficiency
  • Differentiated microbiological structures
20
Q

Factors for Consideration in Reactor Design

A
  • Heat Removal
  • Foam Control
  • Providing oxygen
  • Sterilization
21
Q

_____________: Cellular metabolism produces heat, removed by internal coils or reactor jackets.

A

Heat Removal

22
Q

______________: Cellular metabolism produces compounds that promote foaming. Controlled by mechanical foam breakers and chemical additives.

A

Foam Control

23
Q

______________: Cellular respiration requires oxygen. Sparged air, impeller makes smaller bubbles and increases residence time.

A

Providing Oxygen

24
Q

______________: Single organism desired. Steam and filtering.

A

Sterilization

25
Q

What Factors Limit Size of Reactors?

A

Ability to provide oxygen and remove heat.

26
Q

Reactor Types

A
  1. Stirred-tank
  2. Bubble column
  3. Airlift
  4. Propeller Loop
  5. Jet Loop
27
Q
  • Good oxygen mass transfer
  • High energy requirement for mixing
  • Seal to maintain, keep sterile
A

Agitated tank

28
Q
  • Low shear environment
  • No seal needed
  • Restricted to low viscosity
  • Less mixing than agitated tank
  • Bubble coalescence limits upper air flow rate
A

Bubble Column

29
Q
  • Better mixing than bubble column with same low shear and energy requirements and lack of seal
  • work with higher viscosity liquids than bubble columns
  • Still less mixing than agitated tank
A

Loop reactors

30
Q

__________ breaks bubbles into smaller ones to provide for better oxygen mass transfer

31
Q

_________ are typically glass, commercial fermentors are typically stainless-steel Heat removal/addition is typically by coils along the wall, or a water jacket around the tank.

A

Bench-top tanks

32
Q

_________ prevents foaming problems, but can cause additional mass transfer resistance.

33
Q
  • volume of liquid in tank, does not include head space Seal for agitator shaft must not allow contamination.
A

“working volume”

34
Q

_________ are used to augment mixing and gas dispersion.

35
Q

_____________: disc with 6 to 8 blades. Pumps fluid in a radial direction. Compartmentalization with multiple impellers on a shaft.

A

Rushton impellers

36
Q

_____________: pumps liquid in a vertical direction. Lower energy for the same oxygen

A

Axial flow impeller