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Fed-batch culture of hybridoma cells: comparison of optimal control approach and closed loop strategies
Authors:M de Tremblay  M Perrier  Dr C Chavarie  J Archambault
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. ldquoArdquo, H3C 3A7 Montréal, Québec, Canada
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 - CPR l/(ld) carbon dioxide production rate - D t l/d dilution rate - e t l/d control error - F L/d feed flow rate - Glc mM glucose concentration - Gln mM glutamine concentration - Lac mM lactate concentration - I mg performance index - k d l/d specific death rate - 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 - K glc mM kinetic parameter for growth rate - K gln mM kinetic parameter for growth rate - K tr L/(cell·d) transport coefficient - Kmgr l/d kinetic parameter for Mab production - m glc mM/(cell·d) maintenance coefficient - M Ab mg/l monoclonal antibody concentration - P t covariance matrix - q glc l/(l·cell·d) specific CO2 production rate - q glc mM/(cell·d) specific glucose uptake rate - q gln mM/(cell·d) specific glutamine uptake rate - q Mab mg/(l·cell·d) specific monoclonal antibody production - t f d final culture time - T d sampling rate - u control input - V l reactor volume - X cell/l total cells concentration - X v cell/l viable cells concentration - Y yield coefficient Greek agr mg/cell variable yield coefficient - agr 0 mg/(cell·d) growth-associated kinetic parameter - beta mg/(cell·d) non growth-associated kinetic parameter - gamma t+1 defined by Eq. (19) - lambda forgetting factor - mgr l/d specific growth rate - mgr max l/d specific growth rate - tau i d controller integral time constant
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