1 Anti-slug control on a small- scale two-phase loop Heidi Sivertsen and Sigurd Skogestad Departement of Chemical Engineering, Norwegian University of Science and Technology
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Anti-slug control on a small-scale two-phase loop
Heidi Sivertsen and Sigurd Skogestad
Departement of Chemical Engineering,
Norwegian University of Science and Technology
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Outline
• Introduction
• Experimental set up
• Results anti-slug control
• Controllability analysis
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Slug cycle
1. Liquid build-up
2. Pressure buildup
3. Mass acceleration
4. Liquid fallback
1 2
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Slug cycle Experiments performed by the Multiphase Flow Technology Laboratory, NTNU (prof. Nydal)
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Why is riser slugging undesired?
Slugging leads to:
• Oscillation of separator level, bad separation and in some cases separator flooding.
• Pressure oscillations cause wear and tear on equipment.
• Unnecessary flaring.
• Pressure variations can damage the reservoir.• Reduced production rate.
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How to avoid riser slugging
The traditional solutions have been to change the process either by changing the design:
• Larger separator
• Slug catchers
• Other design changes
Or by changing the operational conditions:
• Increase separator pressure
• Choking to increase riser pressure
Slug catcher
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How to avoid riser slugging
Now: control has become the way to handle the problem. Several tests ans implementations have been carried out:
•Courbot (1996)•Havre, Stornes and Stray (2000)•Hedne and Linga (1990)•Sarica and Tengesdal (2000)
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Experimental mini-loop
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Experimental mini-loop
Valve opening 100%
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Experimental mini-loop
Valve opening 25%
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Experimental mini-loop
Valve opening 15%
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Experimental mini-loop: Storkaas 3-state modelBifurcation diagram
Slugging
No slug
Predicted smooth flow: Desirable but open-loop unstable
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Use of feedback control to stabilize riser slugging
With the use of a feedback loop we can change the dynamics of the system, making it stable where it would not be otherwise!
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Feedback control using PI controller
PCSP
PI controllerGain= -2.5 bara-1
τI = 10s
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Experimental vs theoretical results
Controller on
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Feedback control with topside measurements?
PCSP
Not reported
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Controllability analysis using model
Valve opening Z
0.12 0.25
-20.3411 -35.2145
-0.0197 0.0071 ± 0.1732i
Open loop poles of the system
RHP poles!
Skogestad and Postlethwaite:
For complex RHP- poles, pRHP, each real RHP-zero, zRHP, of the system must approx. obey : zRHP > 2.3 * | pRHP | If not, the system is not stabilizable using feedback control.
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Fig: Measurements andestimates available
P1 P2 ρ FQ Fw
-1.285 46.984 0.092 -3.958 -65.587
0.212 -0.0547 -0.369 ± 0.192i -0.007 ± 0.076i
Zeros of the system for z = 0.25
Controllability analysis using model
P1
P2
FQ
FW
ρ
Requirement for stabilization:
zRHP > 0.4
Requirement for performance:
z >> 0
(both RHP and LHP zeros)
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Conclusion
• Experimental loop analyzed using simple model
• Simple PI controller using inlet pressure P1 stabilizes the flow.
• Not possible using single topside measurement
• Future work: Using only topside measurements
- Cascade control configuration
- ∞ controller
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• Experiments: M.Sc. student Ingvald Baardsen
• Model: Ph.D. student Espen Storkaas
• Finance:
Statoil
The Norwegian Research Council
Acknowledgments
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References
• Courbot (1996). Prevention of Severe Slugging in the Dunbar 16” Myultiphase Pipeline. Offshore Technology conference, May 6-9, Houston, Texas
• Havre, Stornes and Stray (2000). Taming slug flow in pipelines. ABB review 4, 55-63.
• Hedne and Linga (1990). Suppression of Terrein Sugging with Automatic and manual Riser Choking. Advances in Gas-Liquid Flows, pp 453-469.
• Sarica and Tengesdal (2000). A new technique to eliminating severe slugging in pipeline/riser systems. SPE Annual Technical Conference and Exhibition, Dallas, Texas. SPE 63185.
• Storkaas, Godhavn and Skogestad (2003). A low-dimentional model of severe slugging for controller design and analysis. MultiPhase’03, San Remo, Italy, 11-13 June 2003
• Skogestad and Posthletwaite (1996). Multivariable Feedback Control. John Wiley & Sons