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Figure 11. Profile of operating cost under

measurement noise – filter type 2

Again in this simulation (for type 2 filter), a performance improvement is also indicated by the narrowest range achieved of gradient controlled variable (Figure 10) compared to unfiltered (Figure 6) and use of type 1 filter (Figure 8)

Table 5. Operating cost comparison for a 10 h period

Case Studies Cost [$]

Without noise 60487

With noise, without filter 60630 With noise, filter type 1 60590 With noise, filter type 2 60578

5. CONCLUSIONS

Reducing the efforts of measurement noise on plantwide control performance through signal filtering is investigated in this paper. In this work, the self optimizing control structure of Cao (2004) is adopted. It is shown that the calculation of the gradient function can be sensitive to measurement noise and this deteriorates the control performance. Through filtering the process measurements, the self optimising control performance can be improved. Simulation results show that filtering the process measurements used in gradient function calculation can save about $124.8 per day in the total operating cost. This would be significant from a larger capacity and long term operation point of view.

ACKNOWLEDGMENT

This work was supported by Technological and Professional Skills Development Sector Project (TPSDP) – ADB Loan No.1792 – INO. This support is gratefully acknowledged.

REFERENCES

Buckley, P. S. (1964). Techniques of Process

Control. John Willey and Sons, New York.

Cao, Y. (2004), Constrained self-optimizing control via differentiation, In: 7th International

Symposium on Advanced Control of Chemical Processes. Hong Kong.

Heath, J.A., I. K. Kookos., and J.D. Perkins (2000), Process Control Structure Selection Based on Economics. AIChE Journal, v. 46, no. 10, p.1998-2016.

Larsson, T., Govatsmark, M. S., Skogestad, S., and Yu, C. C. (2003). Control structure selection for reactor, separator, and recycle processes.

Industrial & Engineering Chemistry Research, v. 42, no. 6, p. 1225-1234.

Larsson, T, K. Hestetun., Espen Hovland, and Sigurd Skogestad. (2001). Self-Optimizing Control of a Large-Scale Plant: The Tennessee Eastman Process. Industrial Engineering

Chemistry Research, v. 40, p. 4889-4901.

Newell, R. B. a. P. L. L. (1989). Applied Process

Control - A Case Study. Englewood Cliffs,

NJ.

Ogunnaike, B. A. (1996). A contemporary industrial perspective on process control theory and practice. Annual Reviews in Control, v. 20, p. 1-8.

Skogestad, S. (2000). Plantwide Control: The Search for The Self-Optimizing Control Structure.

Journal of Process Control, v. 10, p.

487-507.

Tham, M. T. (1998). Dealing with Measurement noise.

http://lorien.ncl.ac.uk/ming/filter/filter.htm. Wang, P., and T. McAvoy (2001), Synthesis of

Plantwide Control System Using a Dynamic Model and Optimization. Industrial Engineering Chemistry Research, v. 40, p.

Gambar

Figure 11. Profile of operating cost under       measurement noise – filter type 2

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