TY - JOUR N2 - The profitability of chemical processes depends on their design and control. If the process design is fixed, there is little room left to improve control performance. Many commentators suggest design and control should be integrated. Nevertheless, the integrated problem is highly complex and intractable. This article proposes an optimization framework using a dynamic inversely controlled process model. The combinatorial complexities associated with the controllers are disentangled from the formulation, but the process and its control structure are still designed simultaneously. The new framework utilizes a multi-objective function to explore the trade-off between process and control objectives. The proposed optimization framework is demonstrated on a case study from the literature. Two parallel solving strategies are applied, and their implementations are explained. They are dynamic optimization based on (i) sequential integration and (ii) full discretization. The proposed integrated design and control optimization framework successfully captured the trade-off between control and process objectives. UR - http://dx.doi.org/10.1016/j.compchemeng.2012.08.009 ID - discovery10023913 Y1 - 2013/01/10/ JF - Computers & Chemical Engineering PB - PERGAMON-ELSEVIER SCIENCE LTD A1 - Sharifzadeh, M A1 - Thornhill, NF VL - 48 SP - 121 EP - 134 SN - 1873-4375 TI - Integrated design and control using a dynamic inversely controlled process model AV - public KW - Integrated design and control of chemical processes KW - Stochastic mixed-integer dynamic programming KW - Control structure selection KW - Multi-objective optimization KW - MULTIVARIABLE NONLINEAR PROCESSES KW - OUTPUT-FEEDBACK CONTROL KW - FLEXIBILITY ANALYSIS KW - PLANTWIDE CONTROL KW - CHEMICAL-PLANTS KW - CONTROL-SYSTEMS KW - OPTIMIZATION KW - CONTROLLABILITY KW - SELECTION KW - PERSPECTIVE N1 - This version is the author accepted manuscript. For information on re-use, please refer to the publisher?s terms and conditions. ER -