#include <acado_optimal_control.hpp>
#include <acado_gnuplot.hpp>
#include "../integrator/hydroscal_model.hpp"
#include <time.h>
Go to the source code of this file.
Functions | |
USING_NAMESPACE_ACADO void | ffcn_model (double *x, double *f, void *user_data) |
int | main () |
Distillation model 82 diff + 122 alg var Zoltan Nagy, Moritz Diehl, 2000
For a description see e.g. Chapter 7 in the PhD thesis "Real-Time Optimization for Large Scale Nonlinear Processes" (2001) by Moritz Diehl Download at: http://www.ub.uni-heidelberg.de/archiv/1659/
Optimization problem is to steer the column from a disturbed state back into the nominal operating point, minimizing an integrated least-squares deviation of two temperatures and the controls.
EXPRESSIONS: u = ( L_{vol} , Q )^T x = ( X_0, ..., X_{41}, n_1, ..., n_{40} )^T z = ( L_1, ..., L_{40}, V_1, ..., V_{40}, T_0, ..., T_{41} )^T.
Definition in file ocp/hydroscal.cpp.
USING_NAMESPACE_ACADO void ffcn_model | ( | double * | x, |
double * | f, | ||
void * | user_data | ||
) |
Definition at line 62 of file ocp/hydroscal.cpp.
int main | ( | void | ) |
Definition at line 87 of file ocp/hydroscal.cpp.