2003
DOI: 10.1205/026387603322482248
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A Novel MILP Model for Plantwide Multiperiod Optimization of Byproduct Gas Supply System in the Iron- and Steel-Making Process

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Cited by 91 publications
(23 citation statements)
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“…Other studies such as [24,25] focus on the development of mathematical plant models in order to run subsequent optimisation steps in a more efficient and reliable way through MILP -Mixed Integer Linear Programming -solvers or dedicated optimisation modules. For instance, Kim et al [26] suggested a MILP model for plant-wide multiperiod optimisation for the simultaneous optimisation of by-product gasholder level control and by-product gas distribution to determine the optimal fuel load change according to different fuel types. A MILP model was presented also by Kong et al [27] which focuses on reducing total operation cost in the entire energy system of an integrated iron and steel plant for multiperiod operation through optimising by-product gas distribution.…”
Section: Introductionmentioning
confidence: 99%
“…Other studies such as [24,25] focus on the development of mathematical plant models in order to run subsequent optimisation steps in a more efficient and reliable way through MILP -Mixed Integer Linear Programming -solvers or dedicated optimisation modules. For instance, Kim et al [26] suggested a MILP model for plant-wide multiperiod optimisation for the simultaneous optimisation of by-product gasholder level control and by-product gas distribution to determine the optimal fuel load change according to different fuel types. A MILP model was presented also by Kong et al [27] which focuses on reducing total operation cost in the entire energy system of an integrated iron and steel plant for multiperiod operation through optimising by-product gas distribution.…”
Section: Introductionmentioning
confidence: 99%
“…In order to access the maximum load shifting potential of the byproduct gas system, the gasholders are required to fully utilize their storage ability [5,17], and the safety of the gasholders is ensured by constraints defined in Section 3.2.3 [18,19].…”
Section: Problem Statementsmentioning
confidence: 99%
“…Akimoto K early in 1991 on the use of Mixed Integer Programming method established the best gas plant model [2], and Kawasaki, Japan Iron and Steel Plant Optimization byproduct gas distribution and gas counters counter control study; Alberto Bemporad Dr. in 1999 through the Mixed Logical Dynamical Systems Modeling methods applied to the steel plant gas system [3]; Jeong Hwan Kim in 2002, established a steel plant by-product gas distribution and gas counters best counter MILP optimization model for optimal control [4,5], at the same time with the establishment of the optimal model Akimoto compared.…”
Section: Gas Systems Management Researchmentioning
confidence: 99%