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Feedback control overview

Returning to our automobile example and adding the more realistic dimension of disturbances, we see that, in order to ensure we keep a steady r.p.m., we need to be able to adjust the throttle position constantly in order to keep a constant speed. This is essentially the function that cruise control carries out, and is an example of automatic feedback control. Simply put, automatic feedback control provides an automatic adjustment to the FCE in an attempt to maintain the conditions of the process variable at the desired set-point value SP in the presence of disturbances d. [Pg.53]

3 FUNDAMENTALS OF SINGLE INPUT-SINGLE OUTPUT SYSTEMS [Pg.54]

It is interesting to note that if an automatic feedback controller succeeds in keeping the PV at the desired SP in the presence of load disturbances then, by necessity, there will be changes in the MV dictated by the controller. So in effect, proem control takes variability from one place, and moves it to another. Thus, the trick to process control is understanding where variability can be tolerated and where it caimot, and designing schemes that manage variability to acceptable levels. [Pg.54]

1 the process variable PV, which represents the variable that is important to maintain under control  [Pg.55]

4 the controller, whose control law and tuning drive the corrective action and influence the response of the SISO system  [Pg.55]


Fig. 12-11 Cholesterol synthesis and the regulation of HMG-CoA reductase. (A) Overview of the pathway showing negative feedback control of HMG-CoA reductase by cholesterol. Dashed straight arrows denote more than one enzymic reaction. (B) Synthesis of HMG-CoA, in two steps. (C) Details of the conversion of HMG-CoA into isopen-tenyl pyrophosphate, the building block for cholesterol and terpenes (Sec. 12.1). Fig. 12-11 Cholesterol synthesis and the regulation of HMG-CoA reductase. (A) Overview of the pathway showing negative feedback control of HMG-CoA reductase by cholesterol. Dashed straight arrows denote more than one enzymic reaction. (B) Synthesis of HMG-CoA, in two steps. (C) Details of the conversion of HMG-CoA into isopen-tenyl pyrophosphate, the building block for cholesterol and terpenes (Sec. 12.1).
The most important and challenging problems in active and passive stmctural control systems are the formulation and solution of optimal control and nonlinear constrained optimization needed to develop appropriate closed loop feedback control algorithms and the optimal placement, which is the central focus of this book. State-of-the-art techniques for optimal design of passive and active control systems are described in detail in various chapters written by researchers aroimd the world. I welcome this new book for offering a very good overview of the current developments in the field. [Pg.410]

Every efficient microwave reactor to perform chemical syntheses requires reliable temperature measurement as well as continuous power feedback control. Most of the reactors are equipped with temperature monitoring systems, which enable heating of reaction mixtures to a desired temperature without thermal runaways. Moreover, power feedback control systems that are operated in most of the microwave reactors enable a synthesis to be carried out without knowing the dielectric properties and/or conductive properties of all the components of the reaction mixture in detail. An overview of microwave equipment manufacturers and detailed descriptions of microwave reactors can be found in recent review papers and chapters. [Pg.1022]

In this chapter, we consider the design and analysis of feedforward control systems. We begin with an overview of feedforward control. Then ratio control, a special type of feedforward control, is introduced. Next, design techniques for feedforward controllers are developed based on either steady-state or dynamic models. Then alternative configurations for combined feedforward-feedback control systems are considered. This chapter concludes with a section on tuning feedforward controllers. [Pg.273]

Having provided an overview for the need for and basic operation of feedback control, we will now take a closer look at how such control loops are configured. [Pg.56]

Although blood pressure control follows Ohm s law and seems to be simple, it underlies a complex circuit of interrelated systems. Hence, numerous physiologic systems that have pleiotropic effects and interact in complex fashion have been found to modulate blood pressure. Because of their number and complexity it is beyond the scope of the current account to cover all mechanisms and feedback circuits involved in blood pressure control. Rather, an overview of the clinically most relevant ones is presented. These systems include the heart, the blood vessels, the extracellular volume, the kidneys, the nervous system, a variety of humoral factors, and molecular events at the cellular level. They are intertwined to maintain adequate tissue perfusion and nutrition. Normal blood pressure control can be related to cardiac output and the total peripheral resistance. The stroke volume and the heart rate determine cardiac output. Each cycle of cardiac contraction propels a bolus of about 70 ml blood into the systemic arterial system. As one example of the interaction of these multiple systems, the stroke volume is dependent in part on intravascular volume regulated by the kidneys as well as on myocardial contractility. The latter is, in turn, a complex function involving sympathetic and parasympathetic control of heart rate intrinsic activity of the cardiac conduction system complex membrane transport and cellular events requiring influx of calcium, which lead to myocardial fibre shortening and relaxation and affects the humoral substances (e.g., catecholamines) in stimulation heart rate and myocardial fibre tension. [Pg.273]

However, the particle motion depends on the droplet shape and the number of electrodes that the droplet overlays at any given moment. Since this is not known a priori, we use local estimation and control at each time step of our simulation to compute the pressure boundary conditions needed to realize the desired flow field. At each instant in time, the control algorithm is provided with the droplet shape and particle locations, as would be available through a vision sensing system. Any deviation of the particles from their desired trajectories that may arise from thermal fluctuatimis, external disturbances, and actuation errors is corrected using feedback of the particle positions. We now give an overview of our algorithm ... [Pg.486]

Schweickhardt and Allgower in Chapter A3 mainly concentrate on the nonlinearity assessment of processes. A comprehensive overview of general nonlinearity measures and a thorough investigation of the predictive and computational dimension of open loop measures are presented. As the main objective becomes the development of a tool to judge whether a nonlinear controller should be benefieial or needed for a particular process with specific nonlinear characteristics, the controller relevant nonlinearity is quantified. The selected measure is based on the relative differences between the output of nonlinear state feedback law and that of an equivalent linear state feedback law. The controller relevant nonlinearity measure depends not only on the plant dynamics and region of operation but also on the performance criterion used in the derivation of the controller law. [Pg.2]

In Chapter 1 we introduce the concept of SHE (safety, health and environment) information systems. It will provide a frame of reference in our subsequent analysis of the different tools and methods used in accident control through experience feedback. We make a comparison with the human information processes and identify basic similarities and differences. Chapter 2 gives an overview of different boundary conditions of a SHE information system, both inside and outside a company. Chapter 3 introduces four different approaches in safety practice and describes how these will contribute in subsequent parts of the book to our understanding of how to prevent accidents. In Chapter 4 we will look into a case from the environmental field. It demonstrates a successful application of basic principles of experience feedback in the reduction of emissions from a fertiliser plant. We use this example to present some of the issues dealt with in later parts of the book and demonstrate how they form a coherent whole. [Pg.1]


See other pages where Feedback control overview is mentioned: [Pg.53]    [Pg.53]    [Pg.55]    [Pg.53]    [Pg.53]    [Pg.55]    [Pg.76]    [Pg.6]    [Pg.249]    [Pg.525]    [Pg.338]    [Pg.102]    [Pg.6]    [Pg.103]    [Pg.120]    [Pg.36]    [Pg.413]    [Pg.284]    [Pg.173]    [Pg.291]    [Pg.888]    [Pg.66]    [Pg.108]   
See also in sourсe #XX -- [ Pg.53 , Pg.54 , Pg.55 ]




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