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[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
MPC: the idea (born in the ‘70) Reference k+Nc k+Np Process Model prediction Futur Past Control Present : k Morari, M.; Lee, J. L. Model predictive control: past, present and future.  Computers and Chemical Engineering 1999, 23, 667–682
MPC@CB:  what for  ? ,[object Object],[object Object],[object Object]
MPC@CB: for  which   control problem ? ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
MPC@CB:  develop  your  own   next  versions ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
MPC@CB: references(*)  for the  control law used ,[object Object],[object Object],[object Object],[object Object]
MPC@CB: references(*)  with previous  applications ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
PID (regulation) MPC@CB (dynamic optimization + constraint)    Output constraint, with a parameter error MPC@CB: application 1:   powder coating curing   ( Abid et al., 2007 )
PID (régulation)    Output constraint, with a parameter error MPC@CB (dynamic optimization + constraint) ,[object Object],[object Object],[object Object],[object Object],Since the output constraint is saturated, the control move decreases MPC@CB: application 1:   powder coating curing   ( Abid et al., 2007 )
Sublimation time minimization Maximize the sublimation front move H(t) (Contraints on the input) ( Contraint on the output ) Ending condition: stop when  H(t)=L MPC@CB: application 2:   vial   lyophilisation  ( Daraoui  et al., 2007 )
End : H(t)=L MPC@CB: application 2:   vial   lyophilisation  ( Daraoui  et al., 2007 )
Since the output constraint is saturated,  the control move decreases MPC@CB: application 2:   vial   lyophilisation  ( Daraoui  et al., 2007 )
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],MPC@CB:  for  you  ?

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Mpc@Cb Presentation En V2009 03 03

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  • 2. MPC: the idea (born in the ‘70) Reference k+Nc k+Np Process Model prediction Futur Past Control Present : k Morari, M.; Lee, J. L. Model predictive control: past, present and future. Computers and Chemical Engineering 1999, 23, 667–682
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  • 8. PID (regulation) MPC@CB (dynamic optimization + constraint)  Output constraint, with a parameter error MPC@CB: application 1: powder coating curing ( Abid et al., 2007 )
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  • 10. Sublimation time minimization Maximize the sublimation front move H(t) (Contraints on the input) ( Contraint on the output ) Ending condition: stop when H(t)=L MPC@CB: application 2: vial lyophilisation ( Daraoui et al., 2007 )
  • 11. End : H(t)=L MPC@CB: application 2: vial lyophilisation ( Daraoui et al., 2007 )
  • 12. Since the output constraint is saturated, the control move decreases MPC@CB: application 2: vial lyophilisation ( Daraoui et al., 2007 )
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