A general, rigorous dynamic model is described for studying the interaction
s of design and control in a double-effect distillation system. Two approac
hes are adopted. In the first, the steady-state process design and the cont
rol system are optimized sequentially; potential operability bottlenecks ar
e identified and the economic advantage of double-effect systems over conve
ntional single column systems is demonstrated. In the second approach, the
process design and the control system are optimized simultaneously leading
to a more economically beneficial system than that obtained using the seque
ntial approach. (C) 2000 IFAC. Published by Elsevier Science Ltd. All right
s reserved.