Control Input Separation Methods Applied to Cavity Flow

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2008 American Control Conference Westin Seattle Hotel, Seattle, Washington, USA June 11-13, 2008 ThAI01.10 Control Input Separation Methods Applied to Cavity Flow Coşku Kasnakoğlu, Edgar Caraballo, Andrea Serrani and Mo Samimy Abstract Two control input separation methods for controloriented reduced-order modeling of flow systems are developed and implemented in a cavity flow experimental facility. The proposed methods are 1) actuated POD expansion with stochastic estimation and 2) optimization on a Hilbert space, respectively. These methods extend the baseline flow model through the use of innovation vectors, which capture the distance of the actuated flow from the baseline space. This technique remedies certain gaps associated with the sub-domain separation method employed in our earlier works by 1) producing models that exactly reduce to baseline case under no input, 2) not requiring an identifiable control region and 3) improving the estimation of the control terms. The methods are evaluated in experiments to test their ability to achieve reconstruction of the flow. Also, the performance of closed loop controllers built from models based on these new techniques are analyzed. It is seen that these controllers perform satisfactorily in terms of resonance peak suppression, and compare favorably over the old one in terms of power consumption. I. INTRODUCTION It is typical for flow control problems that the control input is applied from the physical boundaries of the system. Control of the flow over a shallow cavity is a benchmark example of boundary flow control that is of great interest due to its rich nature and many applications. Cavity flow is characterized by a strong coupling between flow dynamics and acoustics that produces a self-sustained resonance, which is known to cause, among other problems, structural fatigue in weapons bays. The problem of suppressing cavity flow resonance has been researched extensively in the literature, see for instance [1] [3] which include the work of our flow control group at the Gas Dynamics and Turbulence Lab (GDTL) at The Ohio State University (OSU). Having obtained controllers that work successfully in physical experiments, we are currently working on improving our designs and establishing stronger theoretical foundations for the key components of our approach. Towards this goal, we have identified control input separation as one such component in need of improvement. Some previous work on input separation issues includes techniques such as lifting, weak formulation, balanced truncation, and control functions [4] [6]. As for our group, in the past we developed and used the so-called sub-domain separation method (see [7], [8].) This work is supported in part by AFOSR and AFRL/VA through the Collaborative Center of Control Science (Contract F33615-01-2-3154). C. Kasnakoğlu is with the Electrical and Electronics Engineering Department at TO University of Economics and Technology, 06560 Ankara, Turkey. A. Serrani is with the Department of Electrical and Computer Engineering at The Ohio State University, Columbus, OH 43210, USA. E. Caraballo and M. Samimy are with the Department of Mechanical Engineering at The Ohio State University, Columbus, OH 43210, USA. Corresponding author: Andrea Serrani (serrani@ece.osu.edu) There are however, some major issues associated with the sub-domain method: First of all, when the separation is performed after the generation of a POD basis from actuated flow, the model does not reduce itself to the unforced baseline case when the input vanishes. Another issue is the requirement to identify a control region, which can be difficult or impossible in some applications. Finally, a mismatch between the model used for simulation and control design and the behavior of the controlled plant has been typically observed in experiments, due to underestimation of the control vector field in the reduced-order model. In this paper, we propose two control input separation methods that address in part these issues, and present the results obtained on the cavity flow experimental facility at OSU GDTL. Specifically, in Section II we present some motivations behind this work. The new separation approaches are described in detail in Section III. Experimental results on velocity reconstruction and feedback control of cavity flows are discussed in Section IV. Finally, Section V provides some concluding remarks. II. MOTIVATIONS AND ACKGROUND In this section, we will first provide a brief summary of the classical POD/GP approach to reduced-order modeling of cavity flow; we then present the sub-domain approach used previously to achieve control input separation. A. Classical POD/GP ased Modeling The dynamics of the cavity flow process over a domain Ω R 2, is described by the compressible Navier-Stokes equations governing the spatio-temporal evolution of the flow velocity in the stream-wise and vertical direction, u(x,t) = (u(x,t), v(x,t)), and the local speed of sound, c(x,t). These equations can be expressed in compact form as the evolutionary equation q = X(q) := C + L(q) + Q(q, q) (1) where q := (u, v,c) is the augmented flow velocity, C is a constant, L(q) is linear in q, and Q(q, q) is quadratic in q [9]. Let H be a real Hilbert space with inner product, : H H R such that q : Ω R + R 3, q(, t) H, q(x, ) C k and k N. Let q k (x) = q(x,t k ) be a snapshot taken at time t k and let {q k } M k=1 H be an ensemble of M N snapshots collected at times {t k } M k=1. Let q 0 := E[q j ] where E is a linear averaging operation E[q j ] = M 1 M i=1 w jq j for some weights w j. From the snapshots {q k } M 1, the POD procedure is used to obtain a set of POD modes {φ i } N 1 H 978-1-4244-2079-7/08/$25.00 2008 AACC. 1935 Authorized licensed use limited to: ULAKIM UASL - TO Ekonomi ve Teknoloji Univ. Downloaded on July 01,2010 at 16:46:42 UTC from IEEE Xplore. Restrictions apply.

1936 Authorized licensed use limited to: ULAKIM UASL - TO Ekonomi ve Teknoloji Univ. Downloaded on July 01,2010 at 16:46:42 UTC from IEEE Xplore. Restrictions apply.

1937 Authorized licensed use limited to: ULAKIM UASL - TO Ekonomi ve Teknoloji Univ. Downloaded on July 01,2010 at 16:46:42 UTC from IEEE Xplore. Restrictions apply.

1938 Authorized licensed use limited to: ULAKIM UASL - TO Ekonomi ve Teknoloji Univ. Downloaded on July 01,2010 at 16:46:42 UTC from IEEE Xplore. Restrictions apply.

1939 Authorized licensed use limited to: ULAKIM UASL - TO Ekonomi ve Teknoloji Univ. Downloaded on July 01,2010 at 16:46:42 UTC from IEEE Xplore. Restrictions apply.

SPL (d) SPL (d) SPL (d) (a) M1F4 M032 M1F4 M1Wn 0 2000 3000 4000 5000 6000 7000 8000 00 00 (c) M1Wn M32 M2F1F4 SPL (d) SPL (d) SPL (d) M1F1F4 (b) M1F1F4 M032 M2F4 (d) M2F4 M32 M2Wn projection onto the baseline flow. The new methods provide important improvements over the previously developed subseparation method, such as reducing the model exactly to the baseline under no input, not requiring an identifiable control region, and providing improved estimates for the magnitudes of control derivatives. The new methods were then applied to the OSU GDTL cavity flow experiment where they were evaluated first in their ability to reconstruct actuated flows at the POD level. It was observed that the models improved over existing results in their ability to reconstruct a wide range of flows that are different from the modeling conditions, especially when built from white noise excitation. Next, we tested LQR controllers derived on the basis of the models obtained from the new separation methods. Experimental results showed that these controllers significantly reduce the resonant peak of the single-mode Mach 0.3 flow, for which they were designed, and also performed satisfactorily for off-design conditions at Mach 0.32. This outcome is comparable to what was achieved in previous studies in terms of peak reduction, but is superior in terms of the ratio between overall sound pressure level and mean input voltage. (e) M2F1F4 M32 (f) M2Wn M32 Fig. 7. SPL under LQ control for models built with M1 and M2 at the design condition M = 0.30, and at an off design conditions M = 0.32 OASPL 0 1 2 3 4 5 6 Mean OASPL, M = 0.30 M0 M0Wn M1Wn M2Wn M0F1F4 M1F1F4 M2F1F4 1.5 2 2.5 3 3.5 4 4.5 5 5.5 6 V rms (a) M=0.30 OASPL 0 1 2 3 4 5 6 Mean OASPL, M = 0.32 M0 M0Wn M1Wn M2Wn M0F1F4 M1F1F4 M2F1F4 1.5 2 2.5 3 3.5 4 4.5 5 5.5 6 V rms (b) M=0.32 Fig. 8. Rms voltage vs. average OASPL for several models at different Mach numbers: a) M = 0.3 (design condition) b) M =0.32 (off-design condition) is that models based on the new separation method required less power to achieve similar or better attenuation of the SPL. This is true for both Mach number considered in this study. Secondly, results seem to indicate that the model based on the white noise achieves the best overall performance, noticeably model M1Wn. The model based on M2 seems to perform better for the F1-F4 forcing case; this could be related to small values for the control mode, which in turns require a higher control magnitude to affect the flow. REFERENCES [1] L. N. Cattafesta, D. R. Williams, C. W. Rowley, and F. S. Alvi. Review of active control of flow-induced cavity resonance. In 33rd AIAA Fluid Dynamics Conference, Orlando, FL, 2003. [2] C.W. Rowley and D.R. Williams. Dynamics and control of highreynolds-number flow over open cavities. Annual Review of Fluid Mechanics, 38:251 276, 2006. [3] M. Samimy, M. Debiasi, E. Caraballo, A. Serrani, X. Yuan, J. Little, and J. H. Myatt. Feedback control of subsonic cavity flows using reduced-order models. Journal of Fluid Mechanics, 579:315 346, 2007. [4] M. Hogberg, T. R. ewley, and D. S. Henningson. Linear feedback control and estimation of transition in plane channel flow. Journal of Fluid Mechanics, 481:149 175, 2001. [5] R Chris Camphouse. oundary feedback control using Proper Orthogonal Decomposition models. Journal of Guidance, Control, and Dynamics, 28:931 938, 2005. [6] D.A. Lawrence, J.H. Myatt, and R.C. Camphouse. On model reduction via empirical balanced truncation. In Proceedings of the 2005 American Control Conference, pages 3139 3144, Portland, Oregon, 2005. [7] M. O. Efe and H. Ozbay. Low dimensional modelling and Dirichlet boundary controller design for urgers equation. International Journal of Control, 77(10):895 6, July 2004. [8] E. Caraballo, X. Yuan, J. Little, M. Debiasi, P. Yan, A. Serrani, J. Myatt, and M. Samimy. Feedback control of cavity flow using experimental based reduced order model. In Proceedings of the 35th AIAA Fluid Dynamics Conference and Exhibit, Toronto, ON, 2005. AIAA Paper 2005-5269. [9] C. W. Rowley, T. Colonius, and R. M. Murray. Model reduction for compressible flows using POD and Galerkin projection. Physica D, 189(1-2):115 29, 2004. [10] E. Caraballo, J. Little, M. Debiasi, and M. Samimy. Development and implementation of an experimental based reduced-order model for feedback control of subsonic cavity flows. Journal of Fluids Engineering, 129:813 824, 2007. V. CONCLUSIONS In this paper we presented the development of two new control input separation methods for feedback flow control. The methods incorporate the control input through additional modes obtained from innovation between forced flow and its 1940 Authorized licensed use limited to: ULAKIM UASL - TO Ekonomi ve Teknoloji Univ. Downloaded on July 01,2010 at 16:46:42 UTC from IEEE Xplore. Restrictions apply.