An efficient MILP framework for integrating nonlinear process dynamics and control in optimal production scheduling calculations

Journal Article · 28 November 2017 · Computers and Chemical Engineering

DOI: https://doi.org/10.1016/j.compchemeng.2017.11.021 · OSTI ID:1605935

Kelley, Morgan T. ^[1]; Pattison, Richard C. ^[1]; Baldick, Ross ^[1]; Baldea, Michael ^[1]

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1. Univ. of Texas, Austin, TX (United States)

The emphasis currently placed on enterprise-wide decision making and optimization has led to an increased need for methods of integrating nonlinear process dynamics and control information in scheduling calculations. The inevitable high dimensionality and nonlinearity of first-principles dynamic process models makes incorporating them in scheduling calculations challenging. In this work, we describe a general framework for deriving data-driven surrogate models of the closed-loop process dynamics. Focusing on Hammerstein–Wiener and finite step response (FSR) model forms, we show that these models can be (exactly) linearized and embedded in production scheduling calculations. The resulting scheduling problems are mixed-integer linear programs with a special structure, which we exploit in a novel and efficient solution strategy. A polymerization reactor case study is utilized to demonstrate the merits of this method. Finally, our framework compares favorably to existing approaches that embed dynamics in scheduling calculations, showing considerable reductions in computational effort.

• Research Organization: Univ. of Texas, Austin, TX (United States); Univ. of Texas at Austin, TX (United States)
• Sponsoring Organization: USDOE Office of Electricity (OE); National Science Foundation (NSF)
• Grant/Contract Number: OE0000841
• OSTI ID: 1605935
• Alternate ID(s): OSTI ID: 1549167; OSTI ID: 1872913
• Journal Information: Computers and Chemical Engineering, Vol. 110, Issue C; ISSN 0098-1354
• Publisher: ElsevierCopyright Statement
• Country of Publication: United States
• Language: English