G3 : Bioreactor operations and scale up

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38 Terms

1
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what are challenges with scale-up challenges

  • changes in volume to surface ratio

2
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what are some scale up rules?

keep following parameters constant

  • power input (Pg/V)

    • constant oxygen transfer rate

  • speeds at impeller tip

    • constant maximum shear

3
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Explain the complexity of systems of variables

  • T, DO and pH control

    • setpoints, sensors, controllers

  • interaction between these and many other variables making it complex to analyze

4
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What is the proecess from target to market

  1. Discovery

  2. Process Development

  3. Clinical Supply Production

  4. Process Development and scale up

  5. Final Manufacturing Facility, Validation and Licensing

5
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What is the Process Development Group responsible for?

  • process suitable for manufacturing equipment

  • accurately defined in process documents

  • operate properly at plant start up

6
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What is the Manufacturing Group responsible for?

  • equipment work as designed

  • logistics

    • timely startup

    • facilities

    • staff

    • equipment

    • raw materials

  • Implement process as described in process documents

7
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What are frequent problems in process transfers

  • cells do not grow at expected rate

  • product yields lower than expected

  • product less stable than expected

8
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What are the key purposes of agitation?

  • Gas-Liquid Mass Transfer

    • smaller bubbles→ larger surface area

    • dispersing bubbles through the tank

    • maintaining concentration Gradient

  • Liquid-Liquid Mixing

    • mixing of acid/base to maintain pH

    • mixing feed solutions for fed-batch

  • Suspension of Solids

    • insoluble nutrients

    • cell aggregates

    • microcarriers

    • agitation prevents settling

  • cell aggregate size control

    • break up large clumps

    • prevents shear damage by controlling speed

    • balance between fragmentation and stability

9
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Why do smaller bioreactors require external heating?

They lose heat to environment and need jacketed vessels to maintain temperature

10
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What is the primary challenge with scaling up bioreactors

Removing excess heat from mechanical and metabolism processes

11
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What is the purpose of jacketed vessels in bioreactors

Supply heat to the reactor by circulating hot fluids around it

12
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Why is heat removal more critical in larger scale reactors

produce more heat that can accumulate and harm the system

13
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Heat Generation by microbial metabolism and enthalpy

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14
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What physical parameter is aerobic metabolic heat most closely correlated with?

Oxygen uptake rate (OUR).

15
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Why is oxygen uptake rate used to estimate metabolic heat in aerobic fermentations?

Because it's easier to measure than heat directly and correlates well with metabolic activity.

16
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How can oxygen uptake rate guide bioreactor heat exchanger design?

By estimating heat evolution from the OUR to size the heat exchanger accordingly.

17
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Write the empirical relationship between volumetric heat evolution and oxygen uptake rate?

units:

f - kcal/Lh, o2 - mmol/Lh

<p>units: </p><p>f - kcal/Lh, o2 - mmol/Lh</p>
18
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Why is it important to reduce pCO₂ in mammalian cell cultures?

Because high CO₂ levels can harm cells and affect product quality.

19
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Why is NaHCO₃ removed from the medium?

Because it contributes to CO₂ buildup.

20
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What two buffering agents replaced NaHCO₃ in this strategy?

MOPS and histidine buffer

21
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What is the benefit of using Na₂CO₃ instead of NaHCO₃ as a base?

Na₂CO₃ neutralizes more H⁺ per mole and produces less CO₂.

22
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Why is NaOH not used in mammalian cell cultures?

It causes transient pH spikes that lead to cell aggregation.

23
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What is the main difference between radial and axial flow impellers?

Radial impellers pump fluid outward; axial impellers pump fluid along the shaft axis.

24
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Why is the Rushton impeller less suitable for large-scale reactors?

  • slows top-down mixing

  • leads to poor base mixing

25
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What is one advantage of the axial flow hydrofoil impeller over the Rushton type?

It requires less energy for the same oxygen transfer.

26
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What power number is typical for Rushton and hydrofoil impellers, respectively?

Rushton: ~5; Hydrofoil: ≤ 1

27
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What is the formula for power number dependence on impeller type

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28
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list different impeller power numbers

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29
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Why does scale-up present challenges in bioprocessing?

surface-to-volume ratio decreases, making it hard to replicate physical conditions like heat and mass transfer.

30
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Why is Pg/V often kept constant during scale-up?

To maintain a constant oxygen transfer rate (OTR).

31
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What does keeping impeller tip speed constant help maintain?

Constant maximum shear stress.

32
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What variable is often kept constant to preserve kLa during scale-up?

N3D2

33
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What are primary Variables?

  • pH

  • DO

34
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What secondary variables are affected by efforts to control primary variables?

  • CO2 Accumulation

  • Osmolality ( salt concentration)

  • bubble-burst shear

  • mixing time

  • hydrodynamic shear

35
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who is responsible for process transfer accountability?

  • process development group

  • manufacturing group

36
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What is the process development group responsible for?

  • process must be suitable for larger-scale equipments

  • clear and complete process documentation

  • Process works properly at plant start up

37
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What is the manufacturing group responsible for?

  • process equipment will work as designed

  • logistics in place for timely startup

    • facilities, staff, equipment, raw materials

  • implement process as described in process documents

38
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What is the investigation and resolution game plan for startup problems?

  1. collect all data and samples relating to the problem

  2. make a list of hypothesis as to what could have happened

  3. perform experiments and analyses to isolate the potential sources of the problem