2021
DOI: 10.1016/j.compchemeng.2021.107361
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Refinery production planning optimization under crude oil quality uncertainty

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Cited by 25 publications
(15 citation statements)
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“…To prevent this, Equation (16) prescribes that the amount of inventory EOD u,T within tank u U IT at the end of the final time period T must be equal to the stock EOD u,0 at the beginning of the planning horizon (t = 0). Upper and lower limits on the stock EOD u,t of a tank u U IT are imposed via Equation (17).…”
Section: Multiperiod Formulationmentioning
confidence: 99%
See 1 more Smart Citation
“…To prevent this, Equation (16) prescribes that the amount of inventory EOD u,T within tank u U IT at the end of the final time period T must be equal to the stock EOD u,0 at the beginning of the planning horizon (t = 0). Upper and lower limits on the stock EOD u,t of a tank u U IT are imposed via Equation (17).…”
Section: Multiperiod Formulationmentioning
confidence: 99%
“…Li, Misener, and Floudas 16 applied a robust optimization framework to a nonlinear crude‐oil scheduling problem under demand uncertainty. Li et al 17 formulated a two‐stage stochastic blending problem, where the first‐stage feedstock quantities are optimized under uncertainty in the crude‐oil properties. They sampled a finite number of discrete scenarios via the random vector sampling approach.…”
Section: Introductionmentioning
confidence: 99%
“…The production planning problem has subsequently been solved using many approaches, for instance, linear programming [15] and nonlinear programming [16], based on the considered conditions, such as random parameters. According to studies by Yazdani et al [17]- [20, sustainability problems could also be solved by implementing multiobjective optimization models.…”
Section: Introductionmentioning
confidence: 99%
“…Nevertheless, various uncertainties in the data still exist in practical situations and are ignored by deterministic modeling approaches . The uncertainties include inherent properties (e.g., kinetic rates, heat transfer constants, blending effects, and intermolecular forces), process operation fluctuations (e.g., recipe variations, temperatures, and equipment efficiencies), , and stream properties (e.g., density, sulfur content, and composition), as well as external uncertainties, such as resources, prices, and demand. , …”
Section: Introductionmentioning
confidence: 99%