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Optimal scheduling of single stage batch plants with direct heat integration
Affiliation:1. Automation Technology, BASF SE, 67056 Ludwigshafen, Germany;2. Department of Engineering Cybernetics, NTNU, 7491 Trondheim, Norway
Abstract:This paper addresses the multi-objective optimization problem arising in the operation of heat integrated batch plants, where makespan and utility consumption are the two conflicting objectives. A new continuous-time MILP formulation with general precedence variables is proposed to simultaneously handle decisions related to timing, product sequencing, heat exchanger matches (selected from a two-stage superstructure) and their heat loads. It features a complex set of timing constraints to synchronize heating and cooling tasks, derived from Generalized Disjunctive Programming. Through the solution of an industrial case study from a vegetable oil refinery, we show that major savings in utilities can be achieved while generating the set of Pareto optimal solutions through the ?-constraint method.
Keywords:Energy efficiency  Heat exchanger networks  Short-term scheduling  Multi-objective optimization  Mathematical modeling  Mixed-integer linear programming
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