Özet
In complex real refinery systems, it is essential to find an optimal plan in a short time to maintain operations’ efficiency. An effective tool for industrial use in refinery crude oil scheduling is still lacking. The aim of this study is to develop an optimization tool to support efficient decision-making by ensuring the stability of operations and considering economic profit. An event-based continuous-time Mixed Integer Linear Program is developed to handle crude oil operations from vessels to crude distillation units as well as to satisfy product demands. This new formulation describes real-world operational applications of the TUPRAS Refinery.
Orijinal dil | İngilizce |
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Ana bilgisayar yayını başlığı | Computer Aided Chemical Engineering |
Yayınlayan | Elsevier B.V. |
Sayfalar | 727-732 |
Sayfa sayısı | 6 |
DOI'lar | |
Yayın durumu | Yayınlandı - Oca 2023 |
Yayın serisi
Adı | Computer Aided Chemical Engineering |
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Hacim | 52 |
ISSN (Basılı) | 1570-7946 |
Bibliyografik not
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