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Control principles

Prevention versus Control Principles of pollution prevention How pollution prevention works Pollution prevention auditing Comparing P2 to control options... [Pg.50]

There are many noise-control devices. All, however, rely on one or more of the three basic noise-control principles insulation, absorption and isolation. [Pg.657]

Although the regioselectivity of Friedel-Crafts acylations upon 1-phenylsulfonylpyrrole is ostensibly determined by the "hard-soft" nature of the catalyst <83JOC3214>, this paradigm may not be the controlling principle in determining the regioselectivity of acylations... [Pg.101]

Only one freely definable method is available. Four control principles can be invoked. [Pg.42]

The reliability of measurements plays a pivotal role in food and agricultural areas, particularly in the case of undesirable toxic compounds such as mycotoxins. Quality-control principles for mycotoxin analysis are common to other trace analyses, so good laboratory practices, such as EN 4500, represent the heart of quality assurance requirements. Harmonized Guidelines for Internal Quality Control in Analytical Chemistry Laboratories, published by IUPAC (23), also presents valuable guidelines for the determination of mycotoxins. [Pg.497]

The term feedback mode refers to the coupling of heterogeneous reactions at the specimen and the UME and not to an electronic control principle as commonly used in other scanning probe techniques to maintain a constant sample-probe distance. [Pg.912]

Such devices can be classified according to their measurement and control principles as follows. [Pg.201]

Feed rate controlbased on the carbon dioxide evolution rate (CER) has been shown to be an efficient method. Taherzadeh et al. (14) increased the feed rate stepwise as long as the relative increase in CER was at least 50% of the relative increase in feed rate. Nilsson et al. (13) developed the method further and used the derivative of the CER to control the feed rate. This control principle was very successful in keeping the hexoses at low levels and preventing inhibition from toxic compounds and was the chosen control algorithm in the present work. [Pg.602]

Fig. 11.6 Dimensionless heat generation rates for various values of the dimensionless activation energy. [Reprinted by permission from D. H. Sebastian, Non-Isothermal Effects in Polymer Reaction Engineering, in Temperature Control Principles for Process Engineers, E. P. Dougherty, Ed., Hanser, Munich, 1993.]... Fig. 11.6 Dimensionless heat generation rates for various values of the dimensionless activation energy. [Reprinted by permission from D. H. Sebastian, Non-Isothermal Effects in Polymer Reaction Engineering, in Temperature Control Principles for Process Engineers, E. P. Dougherty, Ed., Hanser, Munich, 1993.]...
Once the precautions that are needed to control exposures are determined, the next step is to compare the level of controls needed against what controls are already in place. There frequently are multiple control strategies that will minimize the potential for exposure. The determination of which control strategy is the best to use is determined by the hierarchy of control principle. Our particular approach to managing risk is to use this hierarchy to evaluate possible risk management approaches for a specific project in conjunction with a modified layer of protection analysis (LOPA) approach.5... [Pg.389]

Table 5.2 summarizes the control principles outlined in this chapter as they apply to the reactor-condenser process. [Pg.125]

Selective value of redox control. For each gene under redox control (principle 4), it is selectively advantageous for that gene to be retained and expressed only within the organelle. [Pg.49]

Level 7 Process-Control System. The key issues of process dynamics and control, namely fresh feed policy and stability in operation of the reaction/separation/ recycle system, are solved at Level 3. Consequently, the implementation of a process-control system may be realized without affecting the basic flowsheet structure, but taking into account fundamental process control principles, as proposed in the methodology developed by Luyben and Tyreus [20]. [Pg.26]

This second-level modeling of the feedback mechanisms leads to nonlinear models for processes, which, under some experimental conditions, may exhibit chaotic behavior. The previous equation is termed bilinear because of the presence of the b [y (/,)] r (I,) term and it is the general formalism for models in biology, ecology, industrial applications, and socioeconomic processes [601]. Bilinear mathematical models are useful to real-world dynamic behavior because of their variable structure. It has been shown that processes described by bilinear models are generally more controllable and offer better performance in control than linear systems. We emphasize that the unstable inherent character of chaotic systems fits exactly within the complete controllability principle discussed for bilinear mathematical models [601] additive control may be used to steer the system to new equilibrium points, and multiplicative control, either to stabilize a chaotic behavior or to enlarge the attainable space. Then, bilinear systems are of extreme importance in the design and use of optimal control for chaotic behaviors. We can now understand the butterfly effect, i.e., the extreme sensitivity of chaotic systems to tiny perturbations described in Chapter 3. [Pg.361]

These are three general control principles utilized in reducing the exposure of workers to occupational health hazards. These involve source controls, transmission barriers, and personal protection. In the first strategy, measures are taken to prevent the release of the toxic contaminant to the air. The second strategy provides means for capturing or blocking the contaminant before it reaches the worker. The final strategy assumes the first two were unsuccessful and requires workers to wear some protective device to prevent contact with the toxic contaminant. [Pg.54]

Systems that have the most potential for reactive distillation are those where the reaction is reversible, heat of reaction is not excessively large, and the products have the correct volatilities in relation to the reactants. Those systems reach chemical equilibrium (i.e., reaction stops) unless the reactants are in large excess or the products are continuously removed. An example system has been reported in the literature by Eastman Chemical (Agreda et al., 1990) for the production of methyl acetate from methanol and acetic acid. The discussion about process operation and the control strategy shown in the paper certainlv adhere to the plantwide control principles we have outlined in this book. [Pg.193]

N.H.Ceglske, "Automatic Process Control for Chemical Engineers, Wiley, NY(1956) 14)Magnus Pyke "Automation, Its Purpose and Future, Philosophical Library, NY(1957) 13)Kirk Othmer, 1st Supplement (1957), 88-103(20 refs) 16)W.G. Holzbock, Automatic Control Principles and Practice, Reinhold,NY(1958) 17)R.L. Cosgtiff, "Nonlinear Control System, McGraw-Hill,NY(1958) 18)D.P.Eckman, "Automatic Process Control, Wiley,NY... [Pg.512]

Accordingly, a dual control principle is provided that acts independently on both parameters. Two methods currently in use are superheated water spray and steam-air mixture. [Pg.3536]

This method validation study indicates that the choice of validation parameters is crucial. Checking the method performance in accordance to the obtained validation results should not be omitted. The preliminary imprecision results do not necessarily predict the analytical variation as the method is taken into routine use. The suitability of system controls have to be considered carefully when patient results are accepted according to the general internal quality control principles. Further, surprisingly high variations should be clarified with the manufacturer. The use of past PT samples is highly recommended to predict the future inaccuracy, whenever... [Pg.106]

Caution must be exercised to minimise errors at every stage of the characterisation. Therefore, quahty assurance/quality control principles must be apphed to sampling, sample storage, sample reconcentration and sample analysis. [Pg.13]

This expression describes the so-called downward control principle (Haynes et al., 1991). It shows that in the extratropics (f 7 0), the vertical velocity w (and hence the vertical transport) at a given... [Pg.113]


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Basic Mechanistic Concepts Kinetic versus Thermodynamic Control, Hammonds Postulate, the Curtin-Hammett Principle

Bimolecular control principles

Chemical reactions, controlling principles governing

Chirality control principles

Control principles dyeing processes

Control principles operation

Control principles system

Controlled Airflow through an Envelope Principles of Natural Ventilation

Controlled-current techniques principles

Downward control principle

Emergencies control principles

Ergonomic principles associated with integration of controls and displays

Field-effect flow control principle

GENERAL PRINCIPLES OF CONTROL

General Principles of Control Charts

General Principles of Optimal Control Theory

Hazard Analysis Critical Control principles

Hazard Control Concepts and Principles

Hazard Control Improvement Principles

Introduction Principles of Controlled Drug Delivery

Level control operating principle

Metabolic control principles

Microworld control principles

Optimal control problem Pontryagin maximum principle

PRINCIPLES OF CONTROL

Particle size, control using chemical principles

Principle of Coherent Control

Principle of Released Electron That Controls Ion-Radical Reactivity

Principle of safety control

Principles of Cell Cycle Control

Principles of Electric-Dipole-Allowed Enantiomeric Control

Principles of controlled crystallization

Quality control principles

Statistical process control basic principles

Stereoelectronic control, the principle

Temperature control, gas principle

The Principles of Quality Control

Threading principle transition-metal-controlled

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