Optimal Synthesis of Sequence of CSTR with Non-Linear Cost Objective Function

Thursday, November 11, 2010: 2:35 PM
250 E Room (Salt Palace Convention Center)
Paul Ghougassian, Chemical Engineering, UCLA, Los Angeles, CA and Vasilios Manousiouthakis, Chemical Engineering Department, University of California at Los Angeles, Los Angeles, CA

In this work, a method is presented that identifies the sequence of mixed flow reactors (CSTR's) which globally minimizes a linear (total residence time) or non-linear (capital cost) objective function, subject to a constraint specifying the terminal concentration of the sequence. Following a review of the relevant literature, the mathematical problem formulation is first presented, and proofs for the existence of the global optimum and for the applicability of the first-order necessary conditions of optimality are provided. The special structure of the resulting equations is then exploited in creating a solution method, which involves exhaustive search in a low dimensional space. For reaction schemes involving reaction rates that are linear in species concentrations, a proof is provided that the optimal sequence of CSTRs consists of identical reactors. Finally, the methodology is illustrated on a number of case studies and conclusions are drawn.

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See more of this Session: Computer-Aided Process Modeling for Design II
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