Quiz 3 - Pt. 2 (Solid state fermentation) Flashcards

1
Q
  • fermentations of solid materials
  • low moisture levels
  • smaller reactor volume
  • low contamination and easy product separation
    ▪ Easy product separation
    ▪ Energy efficiency
    ▪ Differentiated microbiological
    structures
A

Solid-state Fermentations

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2
Q

feed flows through a column packed with immobilized cells

A

Packed column

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3
Q

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

A

Fluidized bed

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4
Q

air bubbles suspend the immobilized cell particles in a reactor

A

Airlift

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5
Q
  • multilayer growth of cells on solid support
  • common in waste water treatment
    ▪ Support materials can be biologically active or inert
A

Biological films

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6
Q

_____ is widely used for enzymes but not for cells

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

A

Covalent binding
good support materials

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7
Q

there is direct contact between nutrient and support materials; high cell loading

A

Physical adsorption

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8
Q
  • animal cell culture
  • cell retention and selective removal of dead cells
  • removal of cell debris and inhibitory by-products
  • high medium use, costs raw materials and sterilization
A

Perfusion culture

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8
Q

________ provide cofactors, reducing power, energy that many enzymatic reactions require

A

Whole cells

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9
Q

Physical Adsorption

selection of suitable support materials is highly based on ______ and _________

A

adsorption capacity;
strength of binding

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10
Q

methods of preparing polymer beads for Physical Entrapment

A

1) Gelation of polymers
2) Precipitation of polymers
3) Ion exchange gelation
4) Polycondensation
5) Polymerization

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11
Q

_____ most widely used method of cell entrapment

▪ Various matrices: porous polymers
(agar, alginate, carrageenan, polyacrylamide, chitosan, gelatin, collagen)
▪ Porous metal screens
▪ Polyurethane
▪ Silica gel
▪ Polystyrene
▪ Cellulose triacetate
* polymer beads

A

Physical entrapment

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12
Q

similar to enzyme immobilization; entrapment and binding

A

Active immobilization

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13
Q

uses biofilm

A

Passive immobilization

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14
Q

multi-layer growth on solid surfaces

A

Biofilm

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15
Q
  • high cell concentrations
  • eliminates cell washout at high dilution rates
  • high volumetric productivities
  • May provide favorable microenvironment
    ▪ Genetic stability
    ▪ Protection from shear damage
  • Major Limitation: Mass transfer (_____) resistances
A

Immobilized cell system
diffusional

16
Q

taken through many feeding cycles, with each feeding cycle followed by a harvest cycle during which the volume is drawn back down to V0 and the cycle begins again

A

Repeated fed-batch

17
Q

Fed-batch Operation

are started as batch cultures and grown to an initial cell concentration X

A

Fed-batch cultures

18
Q

Fed-batch Operation

  • gain some advantages of a CSTR, retain some disadvantages of batch
  • ____reduces substrate inhibition or catabolic repression
  • ____ nature usually leads to higher operations cost and batch variability
A

Fed-batch reactors
Semi-batch nature

19
Q

Multistage chemostat

First ________ is fed with a non-inducing growth substrate, allowing the recombinant strain to be produced

the _____ from the first chemostat feeds a second chemostat that is _______, and the product is produced.

A

Chemostat
Effluent
Fed inducer

20
Q

Special Cases - Chemostat

________ and wild type grow at the same rate if the recombinant product is not expressed

A

Recombinant strain

21
Q

Special Cases - Chemostat

if the recombinant product is expressed, the recombinant strain grows much ________

22
Q

are continually added to the second chemostat not allowing take-over by a fast growing mutant

A

New recombinant cells

23
Q

chemostats cannot be operated if ______

A

Umax < D (dilution rate)

24
Q

What is desired if we have a high volume of feed with a low concentration of substrate?

A

High dilution rate

25
Q
  • is more mechanically reliable and more flexible
  • equations were for cell mass
A

Batch reactor

26
Q

maintaining the organism with the desired characteristics

A

Genetic stability

27
Q

maintaining a sterile system

A

Operability

28
Q

validating the process; initially, many process batch is too expensive to revalidate after clinical trials

A

Regulatory

29
Q

rate of product per time per volume. Chemostat better for growth associated products. Wasted time in batch process.

A

Productivity

30
Q

ability to make more than one product with the same reactor. Batch better.

A

Flexibility

31
Q

maintaining the same conditions for all of the product produced. In theory, chemostat better, steady state.

32
Q

Specialized Reactors

A

▪ Chemostat with recycle
▪ Multistage chemostat
▪ Fed-batch
▪ Perfusion

33
Q

▪ Recombinant product under the
control of an inducible promoter.

A

Special Cases - Chemostat

34
Q

types of immobilization

A

active immobilization
passive immobilization

35
Q

porous support materials causes intraparticle pore diffusion (at high cell densities) and hard to control microenvironmental conditions

A

Disadvantage of Physical Entrapment

36
Q

▪ Analysis similar to immobilized enzymes
▪ Damkohler number
▪ Effectiveness factor
▪ Thiele modulus

A

Diffusional Limitations of bilogical films

37
Q

3 Immobilized Bioreactors

A

▪ Packed-column
▪ Fluidized-bed
▪ Airlift