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Agustriyanto GRDG Analysis of the Alstom Reference 2007

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Figure 3. Process response to step pressure disturbance at 100 % load

Figure 4. Process response to step pressure disturbance at 50% load

Figure 5. Process response to step pressure disturbance at 0% load

REFERENCES

[1] Asmar, BN., Jones, W.E., and Wilson, J.A, “A

process engineering approach to the ALSTOM gasifier problem,” Proceedings of the Institution of Mechanical Engineers Part I - Journal of Systems

and Control Engineering, Vol. 214, No. 16, pp.

441-452, 2000.

[2] Bristol,E, “On a new measure of interaction for

multivariable process control,” IEEE Transaction

on Automatic Control, Vol.11, No.1, pp.133-134,

1966.

[3] Burnham, K., Young, P., and Dixon, R., “Special

issue on the ALSTOM gasifier control engineering

benchmark challenge,” Proceedings of the

Institution of Mechanical Engineers Part I -

Journal of Systems and Control Engineering, Vol.

214, No. 16, 2000.

[4] Chang, J.W., and Yu, C.C., “Relative disturbance

gain array,” AIChE Journal, Vol. 38, No.4,

pp.521-534, 1992.

[5] Chen, D., and Seborg, D.E., “Relative gain array

abalysis for uncertain process models,” AIChE

Journal, Vol. 48, No.2, pp.302-310, 2002.

[6] Dixon, R., and Pike, A.W., “Introduction to the 2nd ALSTOM benchmark challenge on gasifier control,” in Control 2004, Bath, UK.

[7] Dixon, R., Pike, A.W., and Donne, M.S., “The

ALSTOM benchmark challenge on gasifier

control,” Proceedings of the Institution of

Mechanical Engineers Part I - Journal of Systems

and Control Engineering, Vol. 214, No. 16, pp.

389-394, 2000.

[8] Kariwala, V., Skogestad, S., and Forbes, J.F.,

“Relative gain array for norm-bounded uncertain

systems,” Industrial and Engineering Chemistry

Research, Vol.45, No.5, pp.1751-1757, 2006.

[9] Ljung, L, System Identification – Theory for the

Users, Prentice Hall, 1997.

[10]Luyben, W.L., Tyreus, B.D, and Luyben M.L,

Plantwide Process Control, McGraw Hill, New

York, 1998.

[11]Skogestad, S., “Control structure design for

complete chemical plants,” Computers and

Chemical Engineering, Vol. 28, pp.219-234, 2004.

[12]Stanley, G., Marino-Galarraga, M., and McAvoy,

T.J., “Shortcut operability analysis .1. The relative

disturbance gain,” Industrial and Engineering

Chemistry process Design and Development,

Vol.24, No.4, pp.1181-1188, 1985.

Gambar

Figure 3. Process response to step pressure

Referensi

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