Design and Analysis of an Integral Startup System for Distillation Columns
暂无分享,去创建一个
A novel, integral process control system is developed for the complex startup and product changeover processes associated with distillation columns. First, theoretical foundations are considered. A problem decomposition then provides the basis for the systematic development of an automatic, recipe-based procedure. The architecture of the system developed is presented and the manner in which the recipe-based procedure operates is illustrated using experimental results generated by production plant.
[1] G. Wozny,et al. Industrial realization of time-optimal strategies for product changeover operations of coupled distillation columns , 1995 .
[2] Stephen S. Melsheimer,et al. Time-optimal startup control algorithm for batch processes , 1991 .
[3] George Fieg. Composition control of distillation columns with a sidestream by using gas chromatographs , 2002 .