hydroscal.cpp File Reference

#include <acado_optimal_control.hpp>
#include <acado_gnuplot.hpp>
#include "../integrator/hydroscal_model.hpp"
#include <time.h>

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Functions
USING_NAMESPACE_ACADO void	ffcn_model (double *x, double *f, void *user_data)
int	main ()

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Detailed Description

Author:

Boris Houska, Hans Joachim Ferreau, David Ariens

Date:

2009-2010

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.

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Function Documentation

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.