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Optimal output selection for batch processes

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H kon Dahl-Olsen, Sridharakumar Narasimhan. and Sigurd Skogestad ... Look for variables which give small deviation from optimality when controlled at ... – PowerPoint PPT presentation

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Title: Optimal output selection for batch processes


1
Optimal output selection for batch processes
HÃ¥kon Dahl-Olsen, Sridharakumar Narasimhan and
Sigurd Skogestad
2
Outline
  • Batch optimization
  • Implementation schemes
  • Variable selection method
  • Reactor case study
  • Summary

3
Batch optimization
  • Minimum time to given specification
  • Maximum product in fixed time

4
Dynamic optimization
5
Implementation
  • Online optimization measurements used to update
    model
  • Self-optimizing control good outputs give near
    optimal performance

6
Variable selection
  • Unconstrained degrees of freedom
  • Based on Pontryagins minimum principle
  • Look for variables which give small deviation
    from optimality when controlled at fixed
    reference, even under disturbances

7
Maximum gain rule
  • Loss is defined in terms of value of the
    Hamiltonian
  • The loss is time-varying

8
Maximum gain rule
Need to relate variations in inputs to variations
in outputs
9
Maximum gain rule for dynamic optimization
  • Assume the model is scaled such that dymax1

Select ys to minimize the following expression
along the nominal trajectory
10
How to obtain G
  • How does variations in inputs map to the states?
  • Neighboring optimal control gives du(t)K(t)dx(t)
  • We estimate G by

11
Example
Bioreactor
  • Maximize production of product P in a fed-batch
    bioreactor with fixed final time of 150 hours
  • Reaction is driven by the presence of a substrate
    S, which is consumed in the biomass generation
  • The biomass concentration is constrained

Srinivasan, B., D. Bonvin, et al. (2002).
"Dynamic optimization of batch processes II. Role
of measurements in handling uncertainty." Comp.
chem. eng. 27 27-44.
12
Example
Bioreactor
u L/h Sin200 g/L
X lt 3.7 Biomass concentration
S Substrate concentration
P Product concentration
V Volume
u lt 1 Substrate feedrate
Controller
Measurements
13
Example
Bioreactor
X lt 3.7 Biomass concentration
S Substrate concentration
P Product concentration
V Volume
u lt 1 Substrate feedrate
14
Biomass growth rate
Bioreactor
15
Consider gain magnitude
Bioreactor
  • Transformation of input ?vu
  • H?? is constant
  • Minimizing of 1/K2 corresponds to maximizing K2

16
Comparison of gains
Bioreactor
S
X
P
V
17
Simulation results
18
Summary
  • Maximum gain rule extended to dynamics
  • Variational gain from neighboring optimal control
    theory
  • Method works well for a small case study
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