2012
DOI: 10.3182/20120531-2-no-4020.00014
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Controllability analysis of severe slugging in well-pipeline-riser systems

Abstract: Active control of the production choke valve is the recommended solution to prevent severe slugging flow conditions at offshore oilfields. The focus of this work is to find the structure of a simple, yet robust anti-slug control system. In order to find suitable control variables for stabilization, a controllability analysis of the system with different available measurements or different combinations of them was performed. Moreover, for including robustness and performance requirements at the same time, the c… Show more

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Cited by 17 publications
(18 citation statements)
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“…We were able to stabilize the system up to Z = 20% by using nonlinear observers. However, as the valve opening increases, control becomes more difficult [14].…”
Section: A Measuring Top-side Pressurementioning
confidence: 99%
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“…We were able to stabilize the system up to Z = 20% by using nonlinear observers. However, as the valve opening increases, control becomes more difficult [14].…”
Section: A Measuring Top-side Pressurementioning
confidence: 99%
“…Based on a controllability analysis in [3] [14], it is much easier to stabilize the system by using the subsea pressure compared to the top-side pressure. The system could be stabilized up to 40% valve opening by controlling the subsea pressure with a simple PI controller (Fig.…”
Section: B Measuring Subsea Pressurementioning
confidence: 99%
“…Here t is the right normalized eigenvector associated with the unstable RHP pole (p) such that At = pt. For these system models (two dominant conjugated RHP poles) the pole vector can be used as an indication of the input's influence to the output [13]. Tables 3-6 show the values for all the estimated lower controllability boundaries for linearizations at Z = 30%, Z = 45%, Z = 60% and Z = 75%.…”
Section: Lower Boundsmentioning
confidence: 99%
“…However at this point it is uncertain which of these measurements are preferable for control purpose. A comparison carried out in [6,13] concluded that P b is the best controlled variable for single-input-single-output (SISO) control, where w o is preferred if only considering topside measurements, while P t gave the worst results. However in [20] a pressure control comparison was made where it was concluded that P b and P t did equally well as a SISO controlled variable, where P t actually performed best.…”
Section: System Analysismentioning
confidence: 99%
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