Producing proteins on a large scale 2 Flashcards

(36 cards)

1
Q

What are the main stages of cell culture growth?

A

Lag phase, Exponential phase, stationary phase, decline phase

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2
Q

Cell growth is considered a ‘what’ order reaction

A

first order reaction

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3
Q

In the equation

Generation = muX what do the variables represent?

A
mu = Specific cell growth rate
X = the number of cells
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4
Q

What is the Monod kinetic formula?

A

mu = (mumax*X)/(Ks+S)

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5
Q

What is mumax?

A

maximum specific growth rate – represents the cells in exponential phase

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6
Q

What is Ks?

A

The growth- limiting substrate concentrations to give half the µmax

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7
Q

What are the axis of the double reciprocal linear graph used to show monod kinetics?

A

x - 1/S

Y - 1/mu

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8
Q

In the lineweaver burk plot what are the intercepts?

A

X - -1/Ks

y - 1/mumax

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9
Q

In the context of cells what is consumption?

A

Cell death
comsumption = KdX
no cell death is assumed in exponential or lag phase (in batch)
and through continuous reactor

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10
Q

In the context of cell what is Kd?

A

The death constant

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11
Q

If your product is under a constitutive promoter is the product production growth associated?

A

Yes

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12
Q

If your product is under a inducible promoter is the product production growth associated?

A

no - non-growth associated promoter

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13
Q

What is the Leudeking-piret formula?

A

Generation = alphamuX + betaX

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14
Q

With a constitutive promoter what equals zero:

a) alphamuX
b) betaX

A

betaX

- growth associated

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15
Q

How do you determine Yx/s, Yp/s and Ms?

A

Determined by plotting graphs
Yx/s - gradient of X/S graph
Yp/s - gradient of P/S graph
Ms - Qs/mu graph extrapolated back to the y axis

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16
Q

What is Qs?

A

specific utilisation of substrate

17
Q

What scale production might you use a batch reactor for?

A

Small Scale Production

18
Q

What are the limitations of a batch reactor?

A

Expensive because of downtime

Inhibition due to high conc of things cells produce e.g. lactate

19
Q

What cells are often cultured in fed (semi-) batch reactors?

A

Mammalian cells

20
Q

In fed batch the amount of what stays roughly constant?

21
Q

In continuous stirred tank reactors what are the benefits?

A

Constant productivity
Steady state physiology
Control cell growth rate via dilution

22
Q

In what type of bioreactor is there a sensors to ensure that the volume that enters the tank is the same as that leaves the tank?

A

Continuous stirred tank reactor

23
Q

What is the principle of an airlift reactor?

A

Uses airflow to promote mixing.

Air dissolves in medium which get less dense, rises, bubbles burst, gets more dense, sinks

24
Q

What is the benefit of a airlift reactor?

A
No moving parts
Easy to maintain sterility
Allows a large volume 
Low energy input
Low shear
25
What is a labile substrate?
Prone to degradation
26
What are the drawbacks of an airlift reactor?
Large size necessary Hard to maintain homogeneity Needs a lot of air Foaming occurs
27
It airlift reactor batch or continuous?
Batch and occasionally fed-batch
28
What is a wave bag?
A bag ( ~5L) on agitator tipped back and forth to mix medium
29
What is the difficulty of wave bags?
Hard to scale up
30
In exponential phase batch growth what is mu equal to?
mu = mumax
31
What is Kd at exponential phase?
Negliable
32
What assumptions are necessary before exponential phase batch growth?
mu = mumax | Negliable
33
What are the assumptions in a continuous reactor calculation?
Kd=zero | No cells enter the reactor (Xi=0)
34
What is the maximum dilution rate?
The point at which D = mumax
35
What are the Quashi steady state assumptions?
Cells grow a lot and starve before you add substrate – use substrate very quickly M is negligible Non-growth associated protein product is negligible dx/dt = zero dv/dt = zero
36
What what point do you start counting time in a fed batch?
As the substrate is added