Journal article
Operations optimization and control design for a petroleum distillation process
Abstract
Abstract Process automation involves both steady‐state optimization and feedback control. In this paper, the economic optimum steady‐state operating conditions for a petroleum crude distillation process are determined using a tray‐to‐tray model. This model is used to evaluate the steady‐state operation achieved with several multivariable process control designs. Only one controller design was found to result in essentially optimum steady‐state …
Authors
Mizoguchi A; Marlin TE; Hrymak AN
Journal
The Canadian Journal of Chemical Engineering, Vol. 73, No. 6, pp. 896–907
Publisher
Wiley
Publication Date
12 1995
DOI
10.1002/cjce.5450730613
ISSN
0008-4034