This tutorial paper will show that chemical process control parameters
can be obtained from steady state operating data in combination with
simple algebraic equations. The parameters include steady state proces
s gain, feedforward control factor and approximate process time consta
nt. Hen, Lye treat 'self-regulating' processes first. Integrating proc
esses and unstable processes are treated separately, unlike the standa
rd method of setting up linear differential equations followed by Lapl
ace transformations. With the standard method, a steady state portion
of dynamic response, if then is any, appears as a part of equations of
a complex variable. Many control engineers in the chemical industries
who might have studied the method, do not use it because of mathemati
cal difficulties. Instead, they may resort to plant tests that an ofte
n time consuming and costly, The parameters obtained by this paper's m
ethod will aid improvement of control systems. We will address the rel
ation of this method with that of commercial software, which implement
advanced process controls based on plant tests. (C) 1998 Elsevier Sci
ence Ltd.