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Optimization and Computational Fluid Dynamics - Department of ...

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9 CFD-based optimization for papermaking 281<br />

9.4.2 Modeling <strong>and</strong> Optimizing the Complete<br />

Papermaking Process<br />

Although accurate simulation <strong>of</strong> the entire paper machine is still far ahead,<br />

a virtual papermaking line, as we call it, has been developed [20, 22]. It can<br />

be used for papermaking simulation as well as for tailored multi-objective<br />

optimization. The virtual papermaking line combines dissimilar unit-process<br />

models from different disciplines that include mathematical formulas ranging<br />

from simple algebraic equations to CFD models. It also includes models for<br />

moisture <strong>and</strong> heat transfer, <strong>and</strong> for paper quality properties. Simplifications<br />

<strong>of</strong> computationally expensive models are used, for instance, in water removal<br />

which means that an accurate multi-phase flow model <strong>of</strong> the dewatering phenomenon<br />

is replaced with a statistical model based on data produced by the<br />

accurate model. The latter models are especially useful in optimization, when<br />

tens, hundreds or even thous<strong>and</strong>s <strong>of</strong> simulation model evaluations are needed.<br />

We define the virtual papermaking line model as follows<br />

⎧<br />

⎪⎨<br />

⎪⎩<br />

A1(p 1,q 1)=0<br />

A2(p 2,q 1,q 2)=0<br />

.<br />

Anm(p nm,q 1,...,q nm)=0<br />

(9.6)<br />

where Ai for all i =1,...,nm st<strong>and</strong> for the unit-process models, p i ∈ R li<br />

denotes a vector <strong>of</strong> the inputs, <strong>and</strong> q i ∈ R ki is a vector <strong>of</strong> the outputs (model<br />

states) for the i-th unit-process model Ai. We assume here that all the unitprocess<br />

models <strong>and</strong> their outputs are continuously differentiable or if there is<br />

nonsmoothness involved, we assume at least H-differentiability [7].<br />

Based on (9.6) multi-objective optimization problems related to papermaking<br />

process can be determined. Instead <strong>of</strong> the problem formulation (9.5)<br />

we use the following model-based optimization problem formulation<br />

Optimize {f1(x,q 1,...,qnm),...,fnf(x,q 1,...,qnm)} x<br />

�<br />

(9.6)<br />

subject to<br />

x ∈ S<br />

(9.7)<br />

where x ∈ S is a vector <strong>of</strong> the continuous decision variables (also called<br />

control or design variables) which is a selected set <strong>of</strong> the unit-process model<br />

inputs p =(p 1 ,...,p nm ) T . The feasible set S is defined by the box constraints<br />

<strong>of</strong> the decision variables <strong>and</strong> the linear <strong>and</strong> non-linear constraint functions<br />

similarly to (9.5). In (9.7), we ignore those input parameters that are not chosen<br />

as decision variables, because they are constants during the optimization<br />

process. By f1(x, q 1,...,q nm),...,fnf(x, q 1,...,q nm) we denote the objectives<br />

which are to be optimized, i.e., minimized or maximized. Similarly to

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