5 Flashcards

1
Q

Types of bioreactors

A

1) Stirred tank bioreactor
2) Wave bioreactor
3) Bioreactor Process Control and Monitoring
4) Sterilisation and Cleaning of bioreactor

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2
Q

Types of Stirred tank bioreactors

A

1) Stainless steel
2) Single-use

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3
Q

Strategies for operation of bioreactors

A

1) Discontinuous
- Batch
- Fed-batch
2) Continous

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4
Q

Discontinuous bioreactor

A
  • Nothing in,except oxygen for aerobic microbes, antifoam agent, and acid or base to control ph
  • Nothing out until process is terminated
  • limits cell-density due to accumulation of toxic metabolic products and depletion of substrate
  • sometimes, initial substrate may have to be limited due to substrate solubility limits, inhibition and repression.
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5
Q

Fed-batch bioreactor

A
  • substrate is added in increments during fermentation
  • when a liquid feed stream enters the bioreactor, the culture volume is altered
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6
Q

Advantages of fed-batch reactor

A

1) Control concentration of substrate at desired levels
2) Good when controlling concentrations of a nutrient affect the yield of the desired product
3) Longer growth phase
4) Higher cell and/or product concentrations
5) Mode of choice - High product titers

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7
Q

Perfusion

A
  • Cells are separated from the outflow stream and retained inside the bioreactor
  • When substrate concentrations reach critical values, fresh medium is added to the culture system at the same flow rate as the exhausted medium is removed.
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8
Q

Advantages of perfusion

A

1) High cell concentrations
2) Culture over longer periods, even months

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9
Q

Challenges of perfusion

A

1) Reliability of cell retention device
2) Cell viability and/or productivity are not affected

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10
Q

Aerobic bioreactor

A
  • issue with a bioreactor design lies in the provision of adequate mixing and aeration for large proportion of fermentation requiring oxygen.
  • Used for:
    • free and immobilised enzyme reactions
    • culture of suspended and immobilised cells
  • mixing and bubble dispersion achieved by mechanical agitation
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11
Q

Impellers in stirred tank bioreactor

A
  • different shapes and sizes
  • different flow patterns
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12
Q

Baffles in stirred tank bioreactor

A
  • reduce vortexing
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13
Q

Advantages of stirred tank bioreactor

A

1) suitable for batch or continous
2) adequate mixing and aeration
3) good temperature control

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14
Q

Disadvantages of stirred tank bioreactor

A

1) High shear stresses from the impeller may damage sensitive cells

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15
Q

Turndown ratio

A

refers to width of the operational range of a device, and is defined as the ratio of the maximum capacity to minimum capacity.

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16
Q

Why is mixing important?

A

1) blend soluble components in liquid
2) disperse gases through liquid in the form of small bubbles
3) maintain suspension of solid particles such as cells and cell aggregates
4) promote heat transfer to and from liquid
5) disperse immiscible liquids to form an emulsion

17
Q

Factors affecting liquid flow pattern

A
  • impeller design
  • size and geometry of tank
  • properties of the fluid (eg. viscosity)
18
Q

Single-use stirred tank bioreactor

A

Culturing cells in an integral plastic bag that could be mounted within a cylindrical frame to support the bag

19
Q

Wave bioreactor

A
  • used for culture of animal and plant cells, bacteria and viruses.
  • rocking platform in motion creates waves in a culture bag
  • cell culture media
  • cells seeded on micro-carriers as aggregates
20
Q

Principles of wave bioreactor

A
  • Cells and cell culture media contact only a pre-sterile, disposable chamber called the cell bag that rests on a rocking platform
  • Rocking motion induces waves in the cell culture media allowing efficient mixing
  • Single use, requires no cleaning or sterilisation
  • suitable for cultures of up to 500L
21
Q

Biological parameters

A

1) biomass concentration and composition
2) enzyme concentration
3) viability of cells
4) morphology of cells

22
Q

Cell growth monitoring

A
  • cell growth is monitored by manual or automated counting
  • during cell counting, live cells and dead cells can be differentiated by adding a chemical stain
  • 2 parameters obtained from cell counting: viable cell density and viability
23
Q

Methods of monitoring

A

1) On-line monitoring
2) Off-line monitoring

24
Q

On-line monitoring

A

measures parameter directly from process
(ph,temp,dissolved oxygen,flow rate, stirrer speed)

25
Q

Off-line monitoring

A

involves the removal of samples and subsequent measurement
(biomass concentration and composition)
also known as atline analyses

26
Q

Challenges in designing bioprocess controller

A

1) Living organisms are involved
2) Their dynamic behaviour is non-linear and time-varying
3) Complex biological phenomena involving genetic mutation and metabolic variations of cell mass.

27
Q

Proportional controller (P)

A

-output is proportional to error
- greater the magnitude of error, greater the corrective action
- leads to offset

28
Q

Integral controller (I)

A
  • output is determined by the integral of the error over operation time
  • corrective action is slow in the beginning
  • no offset
29
Q

Derivative controller (D)

A
  • output is proportional to the rate of change of error
  • if error is not changing, there is no corrective action