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Cells Growth in Continuous Culture

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Cells Growth in Continuous Culture Continuous culture: fresh nutrient medium is continually supplied to a well-stirred culture and products and cells are ... – PowerPoint PPT presentation

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Title: Cells Growth in Continuous Culture


1
Cells Growth in Continuous Culture
  • Continuous culture fresh nutrient medium is
    continually supplied to a well-stirred culture
    and products and cells are simultaneously
    withdrawn.
  • At steady state, concentrations of cells,
    products and substrates are constant.
  • In batch culture the culture environment changes
    continually.
  • growth, product formation and substrate
    utilization terminate after a certain time
    interval.

2
A continuous-culture laboratory setup
medium
Products, cells
3
Ideal Chemostat
  • Same as perfectly mixed continuous-flow,
    stirred-tank reactor (CFSTR).
  • - Control elements pH, dissolved oxygen,
    temperature
  • - Fresh sterile medium is fed to the completely
    mixed and aerated (if required) reactor.
  • - Suspension is removed at the same rate.
  • - Liquid volume in the reactor is kept constant.

4
Cell Growth in Ideal Chemostat
A material balance on the cell and substrate
concentration around the chemostat yields,
F is the volumetric flowrate of nutrient solution
(l/h) VR is the culture volume (l) (constant)
X is the cell concentration (g/l) P is the
extracellular product (g/l) µg and kd are growth
rate and endogenous rate constant, respectively
(h-1).
qp is the specific rate of extracellular product
formation (g P/g cells-h) Yp/s is the product
yield coefficient (g P/g S).
Subscript 0 denotes the parameters at the feed
medium.
5
Cell Growth in Ideal Chemostat
At steady state, X00, kd 0, qp0 , Monod
equation applied,
0
0
0
0
0
6
Cell Growth in Ideal Chemostat
At steady state, X00, kd 0, qp0 , Monod
equation applied,
Assign. Q 6.13, qo2
Cell Productivity DX
DF/VR, is dilution rate (1/time), the reciprocal
of residence time.
7
Cell Growth in Ideal Chemostat
Washed out If D is set at a value greater than
µm (D gt µm), the culture cannot reproduce quickly
enough to maintain itself.
µm 0.2 hr-1
8
Determination of Monod Parameters
In Chemostat µgD, varying D obtains DS
Chemostat technique reliable, constant
environment, operation may be difficult.
9
Determination of Monod Parameters
Batch X, S, t ? lnX t , get µm (slope) from
data in exponential phase.
10
Cell Growth in Ideal Chemostat
At steady state, X00, kd gt 0, qp0 , Monod
equation applied,
0
0
0
0
11
Cells Growth in Continuous CultureIdeal Chemostat
Endogenous metabolism (X00, kd gt 0, qp0) is
considered Equation summary
Productivities DX
12
Cells Growth in Continuous CultureIdeal Chemostat
Endogenous metabolism (X00, kd gt 0, qp0) is
considered
13
Cells Growth in Continuous CultureIdeal Chemostat
Endogenous metabolism (X00, kd gt 0, qp0) is
considered.
14
Cell Growth in Ideal Chemostat
At steady state, X00, kd gt0, qpgt0 , Monod
equation applied,
0
0
0
15
Cells Growth in Continuous CultureIdeal Chemostat
Endogenous metabolism (kd gt 0, qp gt 0) is
considered
Equation summary
Productivities DP, DX
Use graphical method to determine the optimum DP,
DX.
16
Summary of Growth Kinetics
- Autocatalytic reaction The rate of growth is
directly related to cell concentration Net
specific growth rate (1/time)
- Cell concentration determination - Growth
patterns and kinetics in batch culture - lag
phase - logrithmic or exponential growth phase
- deceleration phase - stationary phase
endogenous metabolism - death phase
17
Summary of Growth Kinetics
  • Effect of factors
  • - Dissolved oxygen

- Temperature, pH, ionic strength, substrate
concentration.
- Heat evolution
18
Summary of Growth Kinetics
- Monod equation
  • Cell growth in continuous culture
  • qp0, kd 0, X00, Monod equation is applied

Productivity DX
19
Summary of Growth Kinetics
  • Cell growth in continuous culture
  • qp0, kd gt0, X00, Monod equation is applied

Productivities DP, DX
20
Summary of Growth Kinetics
  • Cell growth in continuous culture
  • qpgt0, kd gt0, X00, Monod equation is applied

Productivities DP, DX
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