PART 3 Flashcards

1
Q

Types of Reactor

A

Batch and Chemostat (CSTR)

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2
Q

_________: changing conditions - transient (S, X, growth rate), high initial substrate, different phases of growth.

A

Batch

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3
Q

________: steady-state, constant low concentration of substrate, constant growth rate that can be set by setting the dilution rate (ie. the feed flow rate).

A

Chemostat

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4
Q

__________ is more efficient.·

A

Chemostat

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5
Q

____________ is more common.

A

Batch

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6
Q

CHOICE OF CONTINUOUS VS
BATCH PRODUCTION

A

Productivity
Flexibility
Control
Genetic stability
Operability
Economics
Regulatory

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7
Q

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

A

Productivity

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8
Q

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

A

Flexibility

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9
Q

___________: maintaining the same conditions for all of the products produced. In theory, the chemostat is better, steady state. In reality???

A

Control

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10
Q

____________: maintaining the organism with the desired characteristics. Chemostat selects for fast-growing mutants that may not have the desired characteristics.

A

Genetic stability

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11
Q

___________: maintaining a sterile system. Batch better.

A

Operability

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12
Q

____________: validating the process. Initially, many process batch, too expensive to re-validate after clinical trials.

A

Regulatory

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13
Q

Consider the production of a growth-associated product (like cell mass) in _________.

A

suspension culture

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14
Q

__________ of a chemostat is detrimental to engineered organisms.

A

Selective pressure

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15
Q

_______ is more mechanically reliable.

A

Batch

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16
Q

_______ system is more more flexible.

17
Q

SPECIALIZED REACTORS

A

Chemostat with recycle
Multistage chemostat
Fed-batch
Perfusion

18
Q

Can we operate a chemostat with a dilutio rate greater than
maximum growth rate?

Why or why not?

A

No

Because the cell growth cannot keep up with how fast the cells are removed from the reactor, and after some time the cells would washout of the reactor.

19
Q

What conditions would we want to opera a chemostat with a dilution rate higher than the maximum growth rate?

A

We want a high dilution rate when we have a high volume of feed with a low concentration of substrate. Waste water treatment has these characteristics.

20
Q

Chemostats ___________ if µmax <D. Higher dilution rates can be achieved with recycling.

A

cannot be operated

21
Q

Recombinant product under the control of an inducible promoter.

A

Special Cases - Chemostat

22
Q

_______________ grow at the same rate if the recombinant product is not expressed.
If the recombinant product is expressed, the ___________________.

A

Recombinant strain and wild type

recombinant strain grows much slower

23
Q

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

The effluent from the first chemostat feeds a second chemostat that is fed inducer, and the product is produced.

Note: new recombinant cells are continually added to the second chemostat not allowing take-over by a fast growing mutant.

A

MULTISTAGE CHEMOSTAT

24
Q

_________ gain some advantages of a CSTR, retain some disadvantages of batch.

A

Fed-batch reactors

variable volume batch reactor

25
Reduces substrate inhibition or catabolic repression, allows for high conversion, and the extension of stationary phase. Semi-batch nature usually leads to higher operation cost and batch variability.
Fed-batch Operation
26
____________ are started as batch cultures and grown to an initial cell concentration X, after which fed-batch operation begins.
Fed-batch cultures
27
Usually, fed-batch cultures are taken through many feeding cycles, with each feeding cycle followed by a harvest cycle during which the volume is drawn back down to Vo and the cycle begun again.
Repeated Fed-batch
28
Substrate is consumed at the same rate it is added.
QUASI-STEADY STATE
29
PERFUSION CULTURE
Animal Cell culture Constat medium flow Cell retention Selective removal of dead cells Removal of cell debris, inhibitory by products High medium use, costs raw materials and sterilization.