3rd Flashcards

1
Q

The function of the disengagement zone in an
airlift fermenter is to

A
  • prevent CO2 rich bubbles from entering the downcomer
  • reduce the velocity of the bubbles
  • reduce liquid loss as aerosols
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2
Q

Stationary phase is described as

A

no further increase in the cell population
after a maximum value

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3
Q

In the accelerated phase, cell starts to

A

increase and the division rate increases to
reach a maximum

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4
Q

The Monod model predicts that the specific
growth rate

A

will increase with the concentration of the growth limiting substrate until it reaches a maximum value

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5
Q

A mixed fermentation is one, which produces

A

both acid and alcohol

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6
Q

The function of a mechanical seal is to

A
  • prevent contaminants entering the reactor
  • prevent cells from leaving the reactor
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7
Q

The phenomenon in which substrates are used in a sequential manner is known as

A

diauxie

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8
Q

The dilution rate, D is defined as (where F = volumetric flow rate, VR= total volume of culture in the reactor and μ specific growth rate)

A

F/VR

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9
Q

Diauxie is

A

the stagewise uptake of nutrients

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10
Q

An open system in which the growth rate is maintained by adding a nutrient (present in
limiting quantities) at the same rate as that medium containing micro-organism is removed is called

A

Chemostat

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11
Q

In the death phase

A

nutrients available for the cells are depleted
and begin to die

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12
Q

The maximum specific growth rate of an
organism depends on

A

medium composition
temperature
pH

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13
Q

Which of the following is not correct for the Monod model and the Michaelis Menten Model

A

a. The Michaelis Menten Model was derived from a curve fitting exercise
b. The Michaelis Menten model was derived from an analysis of the mechanism of microbial growth
c. The Monod model was derived from an analysis of the mechanism of microbial growth

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14
Q

Bubble column reactor has

A

large height to diameter ratio

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15
Q

Why a T-flask used in small-scale cell culture is incubated in a horizontal position

A
  • To save space
  • To increase the surface area of the liquid-air
    interface
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16
Q

An open system in which the growth rate is maintained by the removal and addition of media at such a rate as to maintain a constant cell density is called a

A

Turbidostat

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17
Q

Wash out in steady state fermentation occurs
when

A

dilution rate is higher than the maximum
specific growth rate

18
Q

Fermenter should be filled with medium upto

A

75-80%

19
Q

Bacterial growth curve is obtained by plotting

A

log of number of cells versus time

20
Q

When intracellular enzymes of whole cells are to be used in a bio-conversion process, it is often necessary to____________the cells.

A

Permeabilize

21
Q

Heat transfer rates (per unit volume) will be
lowest in

A

Continuous packed bed reactor

22
Q

The function(s) of the draft tube in an airlift
bioreactor is

A
  • to reduce bubble coalescence
  • to improve circulation
  • to even out shear conditions throughout the reactor
23
Q

The Monod Model relates

A

specific growth rate to the substrate
availability

24
Q

The height to diameter ratio (H/D) for the
column fermenters is

A

> 3

25
Q

The high oxygen transfer efficiencies of airlift
bioreactors is due to

A
  • the large aspect ratio of the reactor, which leads to a high gas hold-up
  • the large aspect ratio of the reactor, which leads to a high oxygen solubility at the base of the reactor
  • the draft tube, which reduces bubble
    coalescence in the reactor
26
Q

The maximum specific growth rate (μm) of an organism in batch culture is equal to slope of a plot of

A

In [biomass] against time for exponential
phase data only

27
Q

The region of an airlift bioreactor in which the liquid travels in a downward direction is called the

A

Downcomer

28
Q

Population doubling time, td can be expressed as (where μ is the specific growth rate.)

A

ln2/μ

29
Q

A higher Ks value of Monod’s equation means

A

greater affinities to substrate

30
Q

The increased air flow rate in bubble column fermenter can cause excessive foaming and
high retention of air bubbles in the column which

A

decreases the productivity of the fermenter

31
Q

Which of the following is correct for the prediction of time requirement in a batch fermenter?

A
  • Carrying out experiments
  • Mathematical modelling of the
    fermentation process
32
Q

In an airlift bioreactor, the spent gases released from the liquid are called

A

disengagement zone

33
Q

The contents in jet loop reactor are mixed
through

A

external pumping

34
Q

The specific growth rate (μ) is defined as

A

the rate of individual cells division or increase in their biomass

35
Q

The number of baffles in a standard stirred tank
bioreactor is

A

4

36
Q

In the stationary phase

A

growth rate is equal to death rate

37
Q

Which of the following is an example of a
mathematical model?

A
  • Volume of cuboid = length x breadth x height
  • The Monod Model
  • The Michaelis Menten Equation
38
Q

Biomass concentrations during fermentation is

A
  • diluting the samples to optical density less than 0.3
  • monitored by controlling the changes in biomass concentrations
  • considering that optical density is
    proportional to the surface area of the biomass in the sample
39
Q

Chemostats work on the principle of

A

maintaining uniform nutrients
concentration

40
Q

During the exponential phase the maximum specific growth rate equals specific growth rate as

A

concentration of growth limiting substrate is much greater than the Monod constant