TY - JOUR
T1 - Scheduling and Feed Quality Optimization of Concentrate Raw Materials in the Copper Refining Industry
AU - Song, Yingkai
AU - Menezes, Brenno C.
AU - Garcia-Herreros, Pablo
AU - Grossmann, Ignacio E.
N1 - Publisher Copyright:
© 2018 American Chemical Society.
PY - 2018/8/29
Y1 - 2018/8/29
N2 - Scheduling and feed quality optimization for processing solid concentrates in the copper refining industry may be formulated as a large-scale, discrete-time, nonconvex mixed-integer nonlinear program (MINLP) by including logistics operations and ad-hoc blending constraints. However, to solve this complex problem, the full space MINLP for the blending of solid concentrates of copper and the scheduling of their logistics is partitioned into a mixed-integer linear program (MILP) and a nonlinear program (NLP). The solution strategy considers the relax-and-fix rolling horizon with nearby time window overlaps and the use of multiple MILP solutions applied in a two-step MILP-NLP procedure. Two models are proposed for the flowsheet balances: a split fraction model and a process network model. The results indicate that the split fraction model yields near optimal solutions with a large computational effort, whereas the process network can generate several feasible solutions faster. We present a motivating example and an industrial problem with MILP to NLP gaps close to 0%.
AB - Scheduling and feed quality optimization for processing solid concentrates in the copper refining industry may be formulated as a large-scale, discrete-time, nonconvex mixed-integer nonlinear program (MINLP) by including logistics operations and ad-hoc blending constraints. However, to solve this complex problem, the full space MINLP for the blending of solid concentrates of copper and the scheduling of their logistics is partitioned into a mixed-integer linear program (MILP) and a nonlinear program (NLP). The solution strategy considers the relax-and-fix rolling horizon with nearby time window overlaps and the use of multiple MILP solutions applied in a two-step MILP-NLP procedure. Two models are proposed for the flowsheet balances: a split fraction model and a process network model. The results indicate that the split fraction model yields near optimal solutions with a large computational effort, whereas the process network can generate several feasible solutions faster. We present a motivating example and an industrial problem with MILP to NLP gaps close to 0%.
UR - http://www.scopus.com/inward/record.url?scp=85052295363&partnerID=8YFLogxK
U2 - 10.1021/acs.iecr.8b01512
DO - 10.1021/acs.iecr.8b01512
M3 - Article
AN - SCOPUS:85052295363
SN - 0888-5885
VL - 57
SP - 11686
EP - 11701
JO - Industrial and Engineering Chemistry Research
JF - Industrial and Engineering Chemistry Research
IS - 34
ER -