After the simulation starts, the
feed sources begin sending unstable gas condensate to the stabilization unit according to the specified production plan. The feed then enters the stabilization plant, which consists of two process lines. At the moment, one line is operating in stabilization mode, while the other is operating in deethanization mode. At certain periods, both lines switch to deethanization mode simultaneously, as shown now. This behavior is caused by the limited capacity of the NGL receiving tank farm, which periodically becomes completely full. When both tanks are filled and no additional NGL can be accepted, the plant automatically switches to deethanization mode. If we accelerate the simulation, we can see that as storage capacity becomes available again, one of the process lines returns to stabilization mode, while the other continues operating in deethanization mode.
In addition to the NGL
tank farm, the model includes several other farms. However, due to their large capacities, they do not significantly affect the operation of the process unit. As time progresses, production targets for all product streams are successfully achieved. At the same time, the product dispatch nodes gradually approach one hundred percent completion of the scheduled shipment targets.
This example demonstrates how the Petroleum Refining Library for AnyLogic can be used to model real-world oil refining and gas condensate processing facilities with a high level of detail.