Fed-batch culture of hybridoma cells: comparison of optimal control approach and closed loop strategies |
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Authors: | M de Tremblay M Perrier Dr C Chavarie J Archambault |
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Institution: | (1) Treiber Controls Inc., Toronto, Ontario, Canada;(2) Pulp and Paper Research Institute of Canada, Pointe-Claire, Québec, Canada;(3) Université du Québec à Trois-Rivières, Trois-Rivières, Québec, Canada;(4) École Polytechnique de Montréal Département de Génie Chimique, Campus de l'Université de Montréal, C.P. 6079, Succ. A , H3C 3A7 Montréal, Québec, Canada |
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Abstract: | Control of fed-batch culture of hybridoma cells was investigated based on two approaches optimal control theory and feedback control. Experiments were conducted for both approaches-with a feed enriched in glutamine. The optimal feed trajectory, a decreasing one, yielded a final monoclonal antibody (MAb) concentration of 170 mg/l, a three-fold increase compared to a typical batch operation.The feedback strategy relied on the on-line estimation of the net specific growth rate of cells from the measurement of the CO2 production rate with a mass-spectrometer. A PI controller was then used to maintain the growth rate at a desired value by adjusting the dilution rate to the reactor. For the chosen set-point (0.1 d–1), the final MAb concentration achieved was about 100 mg/1. It was found that there was a delay in the assimilation of the glutamine that should be included in the model to explain the lower MAb production in feedback mode. A higher production can be expected also for a lower set-point in feedback operation.List of Symbols
Amm mM
ammonia concentration
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CPR l/(ld)
carbon dioxide production rate
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D
t l/d
dilution rate
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e
t l/d
control error
-
F L/d
feed flow rate
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Glc mM
glucose concentration
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Gln mM
glutamine concentration
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Lac mM
lactate concentration
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I mg
performance index
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k
d l/d
specific death rate
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K
damm l/(mM · d)
kinetic parameter for death rate
-
K
dgln mM
kinetic parameter for death rate
-
K
dlac l/(mM·d)
kinetic parameter for death rate
-
K
c l
controller gain
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K
glc mM
kinetic parameter for growth rate
-
K
gln mM
kinetic parameter for growth rate
-
K
tr L/(cell·d)
transport coefficient
-
K l/d
kinetic parameter for Mab production
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m
glc mM/(cell·d)
maintenance coefficient
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M
Ab mg/l
monoclonal antibody concentration
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P
t
covariance matrix
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q
glc l/(l·cell·d)
specific CO2 production rate
-
q
glc mM/(cell·d)
specific glucose uptake rate
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q
gln mM/(cell·d)
specific glutamine uptake rate
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q
Mab mg/(l·cell·d)
specific monoclonal antibody production
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t
f d
final culture time
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T d
sampling rate
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u
control input
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V l
reactor volume
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X cell/l
total cells concentration
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X
v cell/l
viable cells concentration
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Y
yield coefficient
Greek
mg/cell
variable yield coefficient
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0 mg/(cell·d)
growth-associated kinetic parameter
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mg/(cell·d)
non growth-associated kinetic parameter
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t+1
defined by Eq. (19)
-
forgetting factor
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l/d
specific growth rate
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max l/d
specific growth rate
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i d
controller integral time constant |
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Keywords: | |
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