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54<br />

tial sensitivity to abrupt changes from the input<br />

ones fluctuations like the water flux, for instance.<br />

Although it is not trivial to demonstrate that<br />

there exists a phenomenology linked to variable<br />

interactions, that sensitivity on the drum level<br />

can be interpreted as that.<br />

IV. PRESSURE TRAJECTORIES VERSUS MODEL<br />

In order to confront data and model, one should<br />

to evaluate (11) and (14) numerically. To this<br />

end, the transfer functions are expressed as orthogonal<br />

polynomials up to 5th order. For all kernels<br />

the central assumption is that of expanding<br />

onto polynomials as follows<br />

Essentially a code was created in FORTRAN<br />

capable to calculate all contribution as given<br />

in (14) for instance. Diverse strategies for simulating<br />

curves like the ones of Fig. 2-3 were<br />

taken. In essence special attention was paid on<br />

the drum pressure as the most representative<br />

variable of the plant to be analyzed. We have<br />

simulated to some extent of error such curve by<br />

using Eq. 11 and 14. The main result is displayed<br />

in Fig. 2 where the Eq. (14) is employed to<br />

approximate the “data” as shown in last of Fig.<br />

1. One can see that the simulation adjusts notably<br />

the “right” curve of drum pressure (please<br />

note that the vertical axis is multiplied by 0.34<br />

in order to recover the values of plant as indicated<br />

in Fig. 1) only when almost all contributions<br />

are considered. These results clearly indicate<br />

us a certain consistency of the hypothesis that<br />

the variable interactions is a serious strategy to<br />

model nonlinear systems with a notable accurately.<br />

By the other hands, it also tells us that<br />

the kernel expansion has a little impact on the<br />

modeling of the drum pressure. Consequently,<br />

one can arrive to state that the non-diagonal<br />

terms does not holds a essential role in contrast<br />

to the diagonal ones which returns valuable information<br />

about the system even under dynamic<br />

evolution, interactions themselves and intrinsic<br />

fluctuations. A 7% of discrepancy is found. This<br />

study would serve to go through the searching<br />

of potential sources of instabilities which would<br />

have negatives consequences at the mass delivery<br />

electricity. Finally, in figure (3) it is shown<br />

the possible scenarios where a low order diagonal<br />

integrals produce clouded system identification<br />

on the drum pressure with systematic error<br />

above the 10%.<br />

Figure 2. Data simulated<br />

against identification curves<br />

for different scenarios of<br />

approxmation. Square<br />

boxes denote the “right”<br />

trajectory, whereas doterror<br />

bars in various colors<br />

the model adjusted in<br />

its most representative<br />

approximations as given in<br />

Eq. (14).<br />

Figure 3. Data simulated against identification curves for<br />

different scenarios of approxmation of Eq. (11-14). Left<br />

panel shows the weakness of model when only Eq. 11<br />

is considered and a few interactions terms are included.<br />

Right panel displays the curves when Eq. 14 is taken and<br />

a various non diagonal terms. In all cases, the diagonal<br />

terms appear to be as a substantial component for drum<br />

pressure identification.<br />

V CONCLUSIONS<br />

In this report the application of diagonal integrals<br />

from a variable interaction formalism aimed for<br />

identifying slow systems have been achieved. Concretely<br />

the drum pressure variable inside a tank<br />

where become mixed the water vapor plus nature<br />

gas necessary to generate turbine power have been<br />

identified. The formalism applied adjusts well to data<br />

in up to 7% discrepancy. In this case, the diagonal<br />

part in third order of interactions is assumed. The<br />

identification is consisting to the real data extracted<br />

from plant. In somewhat the adjustability of model<br />

to data depends strongly on the diagonal terms. The<br />

non diagonal ones add more precision but all of them<br />

are not relevant as a robust scheme of system identification.<br />

ACKNOWLEDGMENT<br />

H. N-Ch would like to thank to Mr. Oscar Rivera from<br />

EDEGEL to whom we appreciated his willing in providing<br />

us data from the combined cycle plant as well<br />

as the lively atmosphere found at the FIEM <strong>UTP</strong>.<br />

REFERENCES<br />

[1] Narasimhan, “Multi-objective input signal design<br />

for plant friendly identification of process systems”,<br />

American Control Conference, 2004. Proceedings<br />

of the 2004, IEEExplore.<br />

[2] Thomas, J, Deville Y,” Fast Blind Separation of<br />

Long Mixture Recordings Using Multivariate Polynomial<br />

Identification”, IEEE Transactions on Signal<br />

Processing, 56 pp.5704-5709 (2008).<br />

[3] Jon Mathews and R. L. Walker, Mathematical<br />

Methods of Physics, 2nd ed., Addison-Wesley Publishing<br />

Company, Inc., pp.68–73.<br />

[4] O. Rivera (Private Communication) and thesis to<br />

submmited at the FIEM-<strong>UTP</strong>-2012.<br />

CIENCIA, CULTURA Y TECNOLOGÍA - UNIVERSIDAD TECNOLÓGICA DEL PERÚ

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