Flow averaging level control (FALC) is employed in several chemical pr
ocesses so that fluctuations in outflow from the process can be attenu
ated against disturbances as well as load changes in inflow to the pro
cess while the level is kept around the setpoint. In this paper, a pra
ctical scheme of designing the FALC is proposed. Assuming that the pro
cess has an integral element, the structure of a level control system
becomes a second order system, which can be specified by the time cons
tant as well as damping constant. The proposed scheme determines these
two values so as to optimize two performance indexes : indexes of lev
el controllability and attenuability of fluctuation in the outflow. Th
e controllability index is defined by the integral of squared error of
the level control and that of attenuability is defined by the integra
l of squared derivative of the manipulated variable, outflow rate. The
damping constant for optimizing performance is derived and it is 1/ro
ot 2 (Relative Damping). The magnitudes of disturbance as well as allo
wable ranges of level fluctuation in both nominal and load change oper
ations are given as the design specifications. By giving specification
s to the controller, an IP controller with a gap function is designed
so as to maintain the optimal damping constant of the control system.
The proposed scheme is applied to industrial plants to illustrate the
validity of the scheme.