Title: Measurement of Bioreactor KLa
1Measurement of BioreactorKLa
2Motivations
- Biotech/pharmaceutical industry employing more
Chemical Engineers - Process Engineering
- Validation
- Management
- Pilot testing
- Scale-up
- 2. Good example of mass transfer at gas-liquid
interface - 3. Experience modeling in both semi-empirical
and factorial methods
3Types of Products
- Natural Products
- Drugs
- Penicillin is early example
- Taxol
- Mupricin
- Cyclosporin A, etc.
- Foods
- Fermented beverages
- Fermented dairy products
4Types of Products
- Transgenic Products
- Gene for a therapeutic protein inserted in
foreign expression system - Factor IX
- a-1-antitrypsin
- EPO
- Antibodies
- antithrombin III
- tissue plasminogen activator (TPA)
- Interferons, etc.
5Expression Systems
- Bacterial Cells
- Fungal Cells
- Plant Cells
- Insect Cells
- Mammalian Cells
6Types of Bioreactors (fermentors)(often depends
on shear senstivity)
- Stirred tank
- Aerobic or Anaerobic (air-sparged if aerobic)
- Most common for bacterial cells
- Bubble or airlift column
- Good for shear-sensitive cells
- Fixed bed systems
- Trickle beds, hollow membrane fiber (mammalian
cells), etc.
7Industrial Stirred Fermenter
8Experimental Apparatus
9Transport in Bioprocess Systems
10Why is KLa Important?
- Dissolved oxygen is an important substrate in
aerobic fermentations. Since oxygen is sparingly
soluble in water, it may be the growth-limiting
substrate in these fermentations. For bacteria
and yeast cultures, the critical oxygen
concentration is about 10 to 50 of the
saturated DO (dissolved oxygen concentration).
11Equation for Transport
Oxygen transfer is usually limited by the liquid
film surrounding the gas bubbles
where mO2 is the rate of oxygen transfer per
volume of bioreactor (mass O2/ L3 t), kL is the
oxygen transport coefficient, L/t, a is the
gas-liquid interfacial area per volume of reactor
L2/L3, kLa is the volumetric oxygen transfer
coefficient 1/t, C is saturated DO (dissolved
oxygen) concentration m/L3 (approx. 7 mg/l at
25 deg. C and 1 atm.), CL is the actual DO
concentration in the liquid m/L3
12Terms affecting rate
- KLa
- What we are trying to determine and correlate
with mixing speed and aeration rate - Two quantities multiplied together
- Liquid side (essentially overall mass transfer
coefficient) - Total area of bubbles in bioreactor
- Cant be separated
13Some Interactions Affecting Oxygen Transport in
Aerobic Systems
14Terms affecting rate
- C (saturation oxygen concentration max
solubility of the gas in liquid) - - Constant at a given T and P
- - Available in tables (see on-line lab
manual) - CL (C(t)) the oxygen concentration at a given
time during the run what we measure - - C- CL driving force
15Experimental Apparatus
16Probe response rate needed to get real CL(t)
value
- Gaseous oxygen dissolves in water at bubble
interface and disperses in the bioreactor - Dissolved O2 crosses probe membrane at tip.
- O2 in probe is sensed and sent to meter
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2
3
Time constant 1/kLa
Time constant 1/kp
Fast
17Some Interactions Affecting Oxygen Transport in
Aerobic Systems
18(No Transcript)
19Data Acquisition
20Calibration Screen