Lecture 5 Flashcards

1
Q

system in which a biological conversion is effected. This definition applies to any conversion involving enzymes, micro organisms, and animal or plant cells

A

bioreactor

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2
Q
  • organisms are cultivated in a controlled manner
  • materials are converted or transformed via specific reactions

Bioreactors are specifically designed to influence metabolic pathways

A

Bioreactors

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3
Q

differ from conventional chemical reactors in that they support and control biological entities and must be designed to provide a higher degree of control over process upsets and contaminations, since the organisms are more sensitive and less stable than chemicals

A

bioreactors

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4
Q

Bioreactions products are formed by three basic processes

A
  1. processes in which the product is made by the cells
  2. processes that produce a cell mass
  3. biotransformations or enzymatic conversions: processes that modify a compound
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5
Q

Bioreactions parameters

A
  • controlled temperature
  • optimum pH
  • water availability
  • gas evolution
  • vitamins
  • salts for nutrition
  • sufficient substrate
  • oxygen
  • product and by-product removal
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6
Q

potential entry for contaminants

A

valves
where stirrer shaft enters the vessel

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7
Q

have a tendency to leak around the valve stem and accumulate broth solids in the closing mechanism

A

common valves

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8
Q

valves are recommended for fermenter construction

A

pinch and diaphragm

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9
Q

without repeated sterilisation cycles are use in valve closure

A

rubber or neoprene capable

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10
Q

the gap between the rotating stirrer shaft and the fermenter body must be ______

A

sealed

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11
Q

Inocula for larger fermentations are transferred from _______

A

smaller reactor

The simplest aseptic transfer method is to pressurise the inoculum vessel using sterile air: culture is effectively blown into the larger fermenter

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12
Q

are fitted to the fermenters to allow removal of broth for analysis

A

sampling ports

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13
Q

The majority of bioreactions are ______

A

batch wise

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14
Q

Common steps of a batch-wise bioreaction

A
  • sterilisation
  • sterile culture medium is inoculated with microorganisms
  • proper mixing keeps the differences in compositio and temperature at acceptable levels
  • if needed, the medium is aerated to provide a continuous flow of oxygen. Gaseous by products formed, such as CO2 are removed
  • an acid, alkalie or buffer solution us added if the ph needs to be controlled/modified
  • to keep foaming to acceptable levels, antifoaming agents may be added when indicated by a foam sensor
  • biomass concentration should remain high
  • sterile conditions being maintained
  • effective agitation so that the distribution of substances in the reaction is uniform
  • temperature
  • creation of the correct shear conditions - high may damage cells, low may lead to flocculation or growth on wall and stirrer
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15
Q

Advantages of batch bioreactors

A
  • reduced risk of contamination or cell mutation, due to a relatively brief growth period
  • lower capital investment when compared to continuous processes for the same bioreactor volume
  • more flexibility with varying product/biological systems
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16
Q

Disadvantages of batch bioreactors

A
  • Lower productivity levels due to time for filling, heating, sterilising, cooling, empty and clearning the reactor
  • Greater expense incurred in preparing several subcultures for inoculation
  • Higher costs for labour and/or process control for this non-stationary process
17
Q

Advantages of the continuous operations

A
  • Increased potential for automating the process
  • Reduced labour expense, due to automation
  • Less time expended in emptying, filling and sterilising the reactor
  • Reduced stress on instruments due to sterilisation
18
Q

Disadvantages of the continuous operations

A
  • minimal flexibility since only slight variations in the process are possible (throughput, medium composition, oxygen concentration, temperature)
  • Mandatory uniformity of raw material quality is necessary to ensure that the process remains continuous
  • Higher investment costs in control and automation equipment, and increased expenses for continuous sterilisation of the medium
19
Q

Need adequate mixing and aeration

A

Aerobic bioreactor

characterised by the need of free oxygen

20
Q

Normally do no need gas sparging or agitation

A

Anaerobic bioreactor

lack of oxygen

21
Q

most common type of aerobic bioreactor

A

stirred tank bioreactor

22
Q

Mixing method mechanical agitation

A
  • baffles are usually used to reduce vortexing
  • application: free and immobilised enzyme reactors
  • High shear forces may damage cells
  • Requires high energy input
23
Q
  • baffles are usually used to reduce vortexing
  • application: free and immobilised enzyme reactors
  • High shear forces may damage cells
  • Requires high energy input
A

Mechanical agitation

24
Q

Mixing method: gas sparging

A
  • simple design
  • good heat and mass transfer
  • low energy input

Gas-liquid mass tranfer coefficients depend largely on bubble diameter and gas hold up

25
Q
  • simple design
  • good heat and mass transfer
  • low energy input

Gas-liquid mass tranfer coefficients depend largely on bubble diameter and gas hold up

A

Mixing method: gas sparging

26
Q

Mixing method: airlift

A
  • compared to bubble column reactors, in an airlift reactors, there are two liquid steams: up flowing and down flowing steams
  • Liquid circulates in an airlift reactors as a result of density difference between riser and downcomer
27
Q
  • compared to bubble column reactors, in an airlift reactors, there are two liquid steams: up flowing and down flowing steams
  • Liquid circulates in an airlift reactors as a result of density difference between riser and downcomer
A

Mixing method: airlift

28
Q

used with immobilised or particulate biocatalysts

Medium can be fed either at the top or bottom and forms a continuous liquid phase

A

packed bed bjocatalysts

29
Q

Another variation of the packed bed reactors. Liquid is sprayed onto the top of the packing and trickles down through the bed in small rivulets

A

Trickle bed reactor

30
Q

when the packed beds are operated in upflow mode the bed expands at high liquid flow rates due to upward motion of the particles

A

fluidised bed reactor

31
Q

have the following functions:
- homogenisation
- suspension of solids
- dispersion of gas-liquid mixtures
- aeration of liquid
- heat exchange

A

Stirred tank bioreactors

32
Q

Within each vessel the impeller is connected to an external motor which drives the stirrer system.

Should create high turbulence to maintain transfer rates but this an also generate considerable shear force

A

Stirred tank bioreactors

33
Q

flat vertical plates whose width is about 1/10 of the vessel diameter

A

baffles

34
Q

aid mixing and mass transfer by increasing turbulence and preventing vortex formation

A

baffles

35
Q

one of the advantages of this type of reactors are elimination of attrition effected generally encountered in mechanical agitated reactors

A

Airlift bioreactors

36
Q

Provide a much lower attrition of solid particles
Can be operated with smaller size particles without the drawbacks of clogging, high liquid pressure drop and bed compaction
Smaller particle size faciliates higher mass transfer rates and better mixing

A

Fluidised bed bioreactors

37
Q

used with attached biofilms especially in wastewater engineering
immobilised biocatalyst is packed in the column and fed with substrate either from top or from bottom
changed flow characteristic due to alterations in the bed porosity during operation

A

Packed Bed Bioreactors

38
Q
A