S. Krejci et al., New control system for crude oil processing improvement of control qualityand plant operability, IND ENG RES, 39(3), 2000, pp. 718-723
Most control loops in many installed control systems use only standard, lin
ear PID controllers. Such situations offer the possibility to improve both
control quality and plant operability without additional investments. The d
esign of the new control system for crude oil processing in the PARAMO refi
nery a.s. in Pardubice, Czech Republic, was divided into three different pa
rts: (1) A new control strategy based on the gain scheduling method for the
pressure control and the feedforward method for the level control has been
proposed for stabilization of the desalter tank. (2) A special ratio contr
oller connected in cascade to the original flow controllers has been used f
or the minimization of the temperature difference between the heated stream
s (not controlled in the original system). (3) A combined feedforward-feedb
ack cascade system has been designed for the feed temperature control. All
proposed systems have been tested and set in operation. it has been proven
that there is outstanding improvement over the original control system in s
tabilization of the output temperature, in simplification of the system ope
rability, and in savings of heating medium.