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Respective control concept

Figure 2 Intermediate in the Rh-catalyzed asymmetric hydrogenation used to explain Achiwa s "Respective Control Concept"... Figure 2 Intermediate in the Rh-catalyzed asymmetric hydrogenation used to explain Achiwa s "Respective Control Concept"...
Using Eqs. (1) and (2), a number of CTs have been analyzed. The slopes of l t)vs. (or the values of l(t) t ) and In I t) vs. t curves have been determined in the initial and later stages of lithium injection/extraction, respectively, to estimate the chemical diffusivity of lithium in the electrode. However, it has been pointed out that there is a great discrepancy between the values of the chemical diffusivity determined by the CT technique using the dijfusion control concept and those values obtained hy other electrochemical techniqnes... [Pg.258]

Although problems of regiochemistry are inherent, the aldol condensation of diketones has found vide application. Typical examples are syntheses of cyclopentenones and cyclohexenones from 1,4- and 1,5-diketones, respectively. The concept is illustrated by a synthesis of jasmone 12 (Eq. (12)) [28] and of the homosteroid derivative 13, the latter arising under thermodynamic control in a Robinson annelation reaction (Eq. (13)) [29]. [Pg.8]

Conservation is a general concept widely used in chemical engineering systems analysis. Normally it relates to accounting for flows of heat, mass or momentum (mainly fluid flow) through control volumes within vessels and pipes. This leads to the formation of conservation equations, which, when coupled with the appropriate rate process (for heat, mass or momentum flux respectively), enables equipment (such as heat exchangers, absorbers and pipes etc.) to be sized and its performance in operation predicted. In analysing crystallization and other particulate systems, however, a further conservation equation is... [Pg.45]

Ultrasound can thus be used to enhance kinetics, flow, and mass and heat transfer. The overall results are that organic synthetic reactions show increased rate (sometimes even from hours to minutes, up to 25 times faster), and/or increased yield (tens of percentages, sometimes even starting from 0% yield in nonsonicated conditions). In multiphase systems, gas-liquid and solid-liquid mass transfer has been observed to increase by 5- and 20-fold, respectively [35]. Membrane fluxes have been enhanced by up to a factor of 8 [56]. Despite these results, use of acoustics, and ultrasound in particular, in chemical industry is mainly limited to the fields of cleaning and decontamination [55]. One of the main barriers to industrial application of sonochemical processes is control and scale-up of ultrasound concepts into operable processes. Therefore, a better understanding is required of the relation between a cavitation coUapse and chemical reactivity, as weU as a better understanding and reproducibility of the influence of various design and operational parameters on the cavitation process. Also, rehable mathematical models and scale-up procedures need to be developed [35, 54, 55]. [Pg.298]

We use a simple liquid level controller to illustrate the concept of a classic feedback control system.1 In this example (Fig. 5.1), we monitor the liquid level in a vessel and use the information to adjust the opening of an effluent valve to keep the liquid level at some user-specified value (the set point or reference). In this case, the liquid level is both the measured variable and the controlled variable—they are the same in a single-input single-output (SISO) system. In this respect, the controlled variable is also the output variable of the SISO system. A system refers to the process which we need to control plus the controller and accompanying accessories such as sensors and actuators.2... [Pg.82]

The text summarises the activities and outcome of the Organic HACCP project (www.organichaccp.org) that was completed in 2005, how a database of critical control points (CCPs) was developed for some representative supply chains and how this was used to define a set of recommendations that were then developed into leaflets with advice to producers, processors, retailers or consumers, respectively. The chapter will thus explain how companies at every step of the production chain can utilise the concepts to improve customer satisfaction in a cost-effective manner. Finally, it will describe an example of implementation in a group of collaborating companies and suggest where additional activities are needed in order to develop the concept further. [Pg.490]

Second, in designing new molecule-based electronic devices, one of the major goals is the precise control of the current flowing between the terminals. Electrochemical molecular junctions allow for control of the potentials of the electrodes with respect to the redox potential of incorporated redox-active molecules with well-defined, accessible, tunable energy states. These junctions represent unique systems able to predict precisely at which applied potential the current flow will take off. Even though the presence of a liquid electrolyte represents a detriment towards possible applications, they provide the concepts for designing molecular devices that mimic electronic functions and control electrical responses. [Pg.110]

The concepts derived in the previous Chapter are applied in practice by means of a case study, describing a pesticide company struggling with the question of how to improve the safety of their operational process further. The control model derived in the previous Chapter is used to analyse both the controlled process and controlling process with respect to its impact on process safety. [Pg.79]

From the results of the case study it is concluded that the concepts presented are suitable for displaying the control process of an operational process and to partly identify control improvement areas. However, modelling an operational process with respect to control loops and affected safety barriers requires some additional refinements to the proposed concepts ... [Pg.88]


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