(117d) Integrated Scheduling for Midstream and Downstream of Oil Refinery Supply Chain
AIChE Spring Meeting and Global Congress on Process Safety
2020
2020 Virtual Spring Meeting and 16th GCPS
23rd Topical Conference on Refinery Processing
Refinery Profitability, Flexibility and Optimization II
Wednesday, August 19, 2020 - 2:10pm to 2:30pm
In this work, a new continuous-time based integrated MINLP model is developed to optimize the scheduling of crude unloading and transfer, refinery manufacturing operation and multi-product pipeline distribution. The scheduling objective is to minimize the total operating cost; meanwhile, operating rules and product specifications, inventory limits, delivery constraints and oil product demands must be satisfied. The scope of this work contains crude unloading and transfer, refinery processing and multi-product pipeline distribution system. The crude unloading and transfer system includes vessels, storage tanks and charging tanks. The refinery includes crude distillation, reforming, cracking, hydrotreating, blending, gas processing, and sulfur recovering facilities. The long-distance pipeline distribution system connecting the refinery tank farm and multiple depots, which transport oil products to different local markets. Overall, the integrated simultaneously scheduling model could provide optimal solutions such as crude vessels unloading, crude transfer profiles, processing stream property and flowrate for unit operations, yield and inventory of various petrochemical products, injection sequence and volume of new batches, oil slugs movement inside pipeline, as well as oil product discharging to multiple depot tanks based on consumer demands. The efficacy of the developed integrated scheduling model is demonstrated by an industrial scale study.
Keywords: Simultaneous scheduling, Crude unloading, Crude transfer, Refinery manufacturing, Multi-product, Pipeline distribution, MINLP
References
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