TY - JOUR
T1 - Variable measurement structures for process control
AU - Romagnoli, Jose
AU - Alvarez, Jesus
AU - Stephanopoulos, George
N1 - Funding Information:
The present work was partly supported by the National Science Foundation, Grant ENG75-111 65-AOI, and by a grant from the Dreyfus Foundation to one of the authors (O.S.).
PY - 1981/2
Y1 - 1981/2
N2 - The idea of using variable measurement structures for chemical process control is an attractive one hut in the past it has encountered significant computational and implcmcntationul difficulties. In the present. work an online sequential analysis of the measurement equations is presented, which allows fur a fast and robust updating of the best measurement st.ruot.uro for the control of several processing systems where updating the measurements’ configuration would result in a robust control behaviour. The present paper develops the theoretical foundations for the concept of the variable measurement structures, and implements it for systems operating in a pacudo steady state or dynamic environment. Furthermore, a strategy is developed for the identification of the optirnurn measurement structure in the presence of disturbances. finally the concept of variable measurement structures is discussed with reference to the control of two processing units of interest to the chemical industry; a distillation column and a tubular chemical reactor.
AB - The idea of using variable measurement structures for chemical process control is an attractive one hut in the past it has encountered significant computational and implcmcntationul difficulties. In the present. work an online sequential analysis of the measurement equations is presented, which allows fur a fast and robust updating of the best measurement st.ruot.uro for the control of several processing systems where updating the measurements’ configuration would result in a robust control behaviour. The present paper develops the theoretical foundations for the concept of the variable measurement structures, and implements it for systems operating in a pacudo steady state or dynamic environment. Furthermore, a strategy is developed for the identification of the optirnurn measurement structure in the presence of disturbances. finally the concept of variable measurement structures is discussed with reference to the control of two processing units of interest to the chemical industry; a distillation column and a tubular chemical reactor.
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U2 - 10.1080/00207178108922923
DO - 10.1080/00207178108922923
M3 - Article
AN - SCOPUS:0019529891
SN - 0020-7179
VL - 33
SP - 269
EP - 289
JO - International Journal of Control
JF - International Journal of Control
IS - 2
ER -