Abstract | ||
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Gas-liquid cylindrical cyclone separators are increasingly used for separation of hydrocarbons in the oil and gas industry. They are favoured for their low weight and compact design. However, a challenge is their small volume, which makes them sensitive to flow variations, which can cause operational and separation problems. Optimal control can improve both operational and separation performance. We extend a newly derived control-oriented model to include continuous separation and use this extended model to propose a nonlinear model predictive control algorithm to improve control and optimize the purity of the gas product. To achieve this, one degree of freedom is freed up by implementing band control of the liquid level. The extended model is qualitatively verified in simulation and the performance of the nonlinear model predictive control algorithm is compared with and without measurement noise and with and without optimization of the gas product purity. |
Year | DOI | Venue |
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2017 | 10.1109/MED.2017.7984097 | 2017 25th Mediterranean Conference on Control and Automation (MED) |
Keywords | Field | DocType |
nonlinear model predictive control,gas-liquid cylindrical cyclone separators,hydrocarbon separation,oil and gas industry,optimal control,one degree of freedom,liquid level band control,gas product purity | Degrees of freedom (statistics),Optimal control,Algorithm design,Computer science,Liquid crystal on silicon,Control theory,Flow (psychology),Separator (oil production),Cylinder,Model predictive control,Control engineering | Conference |
ISSN | ISBN | Citations |
2325-369X | 978-1-5090-4534-1 | 0 |
PageRank | References | Authors |
0.34 | 2 | 2 |
Name | Order | Citations | PageRank |
---|---|---|---|
Kristoffersen, T.T. | 1 | 1 | 1.83 |
Christian Holden | 2 | 4 | 3.90 |