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Distributed control system approach

While this staged approach has long been recognized as deficient, it is defensible from a certain perspective. For example, it would be difficult for the control engineers to specify the instrumentation and the distributed control system (DCS) without knowing exactly what process it was intended for. Similarly, it would make no sense for the process engineers to request a control system design for all those flowsheets... [Pg.11]

Centralized control approach. DCS, distributed control system ESD, emergency shutdown system HMJ, human—machine interface MIS, management information system PU, pro cessing unit SIL, safety integrity level SIS, safety instrumentation system. [Pg.914]

While a dynamic simulator can incorporate some features of control loops, sequences, and the operator interface (e.g., displays and historian), a more practical approach embeds the simulation in the Distributed Control System (DCS) and has an adjustable real-time factor. The process simulator reads the DCS outputs for the... [Pg.34]

Minimization of pollutants from the combustion chamber. This approach consists of designing the engine with improved fuel-air distribution systems, ignition timing, fuel-air ratios, coolant and mixture temperatures, and engine speeds for minimum emissions. The majority of automobiles sold in the United States now use an electronic sensor/control system to adjust these variables for maximum engine performance with minimum pollutant emissions. [Pg.525]

FDA device regulation is focused on the device and the device manufacturer. CLIA, on the other hand, focuses on laboratory quality, including the quality of the laboratory test results provided by the devices used, whether developed in-house or as a test kit in commercial distribution to multiple laboratories. The programs differ substantially in approaches and in data requirements. FDA requires unique submissions for each test under its purview, evaluates both performance and labeling, and requires demonstration of analytical validity and clinical validity as appropriate. CLIA inspects laboratories using a system approach based on key probes of the operating system. CLIA requires a demonstration of analytical performance and quality control but does not require a showing of either clinical validity or clinical utility. [Pg.111]

The entire system is based on a tiered approach where three layers of technology are integrated into the overall treatment system, as illustrated in Chart 2. First, a distributed process control system is network linked to the various component subunits of the waste management system such as pH control, ion-exchange control, tank level control, etc. Next, are the recovery/treatment processes themselves. The final tier is a monitoring system which controls both the performance of the treatment systems and the discharge assurance of the plant effluent... [Pg.248]

This approach makes the system simple to operate. The entire process is automatically monitored, recorded, and controlled. Operators can run the system from the central console, or from the local control units. And because of the distributed control, each of the local units will continue to do its job, and the waste treatment system will continue to function, even if the central control unit should became disconnected or malfunction. The system also includes a modem for remote diagnostics and program maintenance. [Pg.248]

Coughanowr, D. R. Process Systems Analysis and Control, 2nd edn. (McGraw-Hill, New York, 1991). Kuo, B. C. Discrete Data Control Systems (Prentice-Hall, Englewood Cliffs, New Jersey, 1970). Landau, Y. D. Adaptive Control—The Model Reference Approach (Marcel Dekker, New York, 1979). Popovic, D. and Bhatkar, V. P. Distributed Computer Control for Industrial Automation (Marcel Dekker, New York, 1990). [Pg.729]

Finally, a steady 1-D lumped stack model is introduced which uses a 0-D lumped approach for each cell in the stack. The model takes the current and power produced by each cell in the stack as input and predicts the 1 -D temperature distribution across the cells of the stack. Such models have the advantage of faster calculation time and are thus better suited for initial design calculations and control system modeling. In this model, each fuel cell is divided into three components, air channel, fuel channel and solid region (electrodes, electrolyte and the interconnect). The control volumes used for air and fuel channel components are shown by the dashed lines in Figure 5.6. The specie concentrations at the exit of air and fuel channels could be calculated using the mass and specie balances for these control volumes which are in the form... [Pg.144]

Except for the cases where the optimal temperature profile is of the bang-bang type, analytical solutions for axially varying optimal profiles are almost impossible. Denn et. al. (11) used a variational approach for a wide class of distributed parameter systems where the optimizing decisions may enter into the state equations or boundary conditions. When intermediate control is involved, one can only obtain numerical approximations to the optimal solution. [Pg.299]

Hukkanen, E.J. A Systems Approach to the Modeling and Control of Molecular, Microparticle, and Biological Distributions. Ph.D. thesis. University of Illinois at Urbana-Champaign Illinois, 2004. [Pg.870]

The use of solid acid catalysts would eliminate waste disposal problems and allow for more advantageous control of product selectivities. However, rapid deactivation of these solid acid catalysts is a problem that significantly hinders the effective performance and selectivity of these catalysts. We have studied the performance of various solid acid catalysts for their activity/deactivation characteristics and also their shape selective effects. Specifically in the liquid phase system, unlike previous researchers, we have studied the activity/deactivation evolution with time on stream rather than rely on final product distribution only. This approach has allowed us to obtain unique data that clearly describe the deactivation pattern of these catalysts. [Pg.200]

The distributions of isoenzymes of aldolase, LD, and CK in the muscles of patients with progressive muscular dystrophy have been found to be similar to those in the earlier stages of development of fetal muscle. The isoenzyme abnormalities in dystrophic muscle have been interpreted as a failure to reach or maintain a normal degree of differentiation. Isoenzyme patterns in regenerating tissues may also show some tendency to approach fetal distributions. This tendency may result from relaxation or modification of control systems in rapidly dividing cells and may account for some of the isoenzyme changes noted (e.g., in muscle in acute polymyositis). [Pg.197]

The Use of Artificial Intelligence in Distributed Control Model Based Reasoning Approach to Chemical Plant Design Use of Expert Systems in Nuclear Power Plants Application of AI to Management and Analysis Problems... [Pg.147]

Using the transfer function concept, Koppel (1967) derived the optimal control policy for a heat exchanger system described by hyperbolic partial differential equations using the lumped system approach. Koppel and Shih (1968) also presented a feedback interior control for a class of hyperbolic differential equations with distributed control. In an earlier paper Koppel e/ al. (1968) discussed the necessary conditions for the system with linear hyperbolic partial differential equations having a control which is independent of spatial coordinates. The optimal feedback-feedforward control law for linear hyperbolic systems, whose dynamical response to input variations is characterized by an initial pure time delay, was derived by Denn... [Pg.469]

Microcomputer-based subsystems are standard in most computer control systems available today. The digital subsystems are interconnected through a digital communications network. Such systems are referred to as distributed digital instrumentation and control systems because of the network approach used to monitor and control the progress. [Pg.1983]


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