دانلود مقاله ISI انگلیسی شماره 25008
عنوان فارسی مقاله

کنترل پیش بین مدل و برنامه ریزی خطی

کد مقاله سال انتشار مقاله انگلیسی ترجمه فارسی تعداد کلمات
25008 2000 7 صفحه PDF سفارش دهید محاسبه نشده
خرید مقاله
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عنوان انگلیسی
Linear programming and model predictive control
منبع

Publisher : Elsevier - Science Direct (الزویر - ساینس دایرکت)

Journal : Journal of Process Control, Volume 10, Issues 2–3, April 2000, Pages 283–289

کلمات کلیدی
کنترل پیش بین مدل - برنامه ریزی خطی - بهینه سازی -
پیش نمایش مقاله
پیش نمایش مقاله  کنترل پیش بین مدل و برنامه ریزی خطی

چکیده انگلیسی

The practicality of model predictive control (MPC) is partially limited by the ability to solve optimization problems in real time. This requirement limits the viability of MPC as a control strategy for large scale processes. One strategy for improving the computational performance is to formulate MPC using a linear program. While the linear programming formulation seems appealing from a numerical standpoint, the controller does not necessarily yield good closed-loop performance. In this work, we explore MPC with an l1 performance criterion. We demonstrate how the non-smoothness of the objective function may yield either dead-beat or idle control performance.

مقدمه انگلیسی

Model predictive control (MPC) is an optimization based strategy that uses a plant model to predict the effect of potential control action on the evolving state of the plant. At each time step, an open-loop optimal control problem is solved and the input profile is injected into the plant until a new measurement becomes available. The updated plant information is used to formulate and solve a new open-loop optimal control problem. The MPC methodology is appealing to the practitioner, because input and state constraints are explicitly accounted for in the controller. A practical disadvantage is the computational cost, which tends to limit MPC applications to linear processes with relatively slow dynamics. For such problems, the optimal control problem to be solved at each stage of MPC is a convex program. The necessity to solve the optimization problem in real time is especially troublesome for large-scale processes. While efficient software exists for the solution of convex programs, significant improvements are obtained by exploiting the structure of the MPC subproblem. Traditionally model predictive control has been formulated using a quadratic criterion. Part of the popularity of the quadratic criterion from a theoretical standpoint is due to its mathematical convenience. From a numerical standpoint, the quadratic criterion is popular, because the resulting optimization can be cast as a quadratic program. For the unconstrained case, the linear quadratic optimal control problem is solved efficiently using dynamic programming. This solution technique has the desirable property that the computational cost scales linearly in the horizon length N as opposed to cubically for the general least squares solution. While the addition of constraints negates the possibility of a general analytic solution to the optimal control problem, the quadratic program may be structured in an analogous manner to the unconstrained problem, yielding linear growth in the horizon length N. Approaches to structuring the optimal control problem with a linear quadratic objective utilizing sparse matrix methods are available in the literature [2], [18] and [21]. Recently Dave and co-workers [7] have advocated the use of an norm as a performance criterion for MPC. One motivation is that the resulting optimal control problem is cast as a linear program. The solution of a linear program is less computationally demanding than the corresponding solution of a quadratic program of the same size and complexity, so it may be preferable to formulate MPC as a linear program. The concept of using linear programming is not new and has been considered by many authors in optimal control (e.g. [16] and [22]) and in MPC (e.g. [1], [12], [3], [4], [5], [6], [10], [14] and [17]). A review of some MPC research with non-quadratic objectives can be found in the paper by Garcia and co-workers [9]. The main theoretical objection to linear programming formulations is that analytic solutions are generally unavailable due to the non-smoothness of the objective function. The non-smoothness is one of the prime reasons why the analysis of the stability for linear programming formulations has been lacking. Notable exceptions include the works of Keerthi and Gilbert [13], who use an endpoint constraint, Genceli and Nikolaou [10], who consider finite impulse response models, and Shamma and Xiong [20], who provide a numerical test whether a given horizon is sufficiently long to guarantee stability for unconstrained MPC. In this paper we examine linear programming formulations of MPC. We begin our discussion by presenting in Section 2 a stabilizing formulation of MPC with a general lp criterion. In Section 3 we analyze the qualitative properties of MPC with an l1 criterion. Unlike MPC with a quadratic criterion, the choice of the tuning parameters for the l1 formulation may result in appreciably different closed-loop performance. In particular, we demonstrate how the non-smoothness of the objective may yield either dead-beat or idle control performance.

نتیجه گیری انگلیسی

The main contribution of this paper has been to illustrate some of the consequences of using MPC with an lp criterion. Our motivation for studying the lp criterion was that for both l1 and l∞ criterion the resulting optimization can be formulated as a linear program. Linear programming formulations are desirable, because they are computationally less demanding than the standard quadratic programming formulations. Furthermore, theoretical issues such as stability are a straightforward extension of the results available for the quadratic criterion. However, performance issues raise questions concerning the suitability of the lp criterion for MPC. Although possessing desirable theoretical and numerical properties, lp formulations suffer many practical drawbacks. The main consequence of the lp criterion is that it may yield either dead-beat or idle control performance. Both of these types of performance may be unsuitable for process control application. While our arguments have been mostly qualitative, it is evident that the culprit is the non-smoothness of the objective function. The non-smoothness causes the stage cost functions to act as competing exact penalties for the constraints u=0 and y=0. For the scalar system, the behavior is simple to understand. Extending these results to higher dimension systems is more difficult and is currently unresolved.

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