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Chemical reactor operating patterns

Chemical reactors intended for use in different processes differ in size, geometry and design. Nevertheless, a number of common features allows to classify them in a systematic way [3], [4], [9]. Aspects such as, flow pattern of the reaction mixture, conditions of heat transfer in the reactor, mode of operation, variation in the process variables with time and constructional features, can be considered. This work deals with the classification according to the flow pattern of the reaction mixture, the conditions of heat transfer and the mode of operation. The main purpose is to show the utility of a Continuous Stirred Tank Reactor (CSTR) both from the point of view of control design and the study of nonlinear phenomena. [Pg.3]

At some point in most processes, a detailed model of performance is needed to evaluate the effects of changing feedstocks, added capacity needs, changing costs of materials and operations, etc. For this, we need to solve the complete equations with detailed chemistry and reactor flow patterns. This is a problem of solving the R simultaneous equations for S chemical species, as we have discussed. However, the real process is seldom isothermal, and the flow pattern involves partial mixing. Therefore, in formulating a complete simulation, we need to add many additional complexities to the ideas developed thus far. We will consider each of these complexities in successive chapters temperature variations in Chapters 5 and 6, catalytic processes in Chapter 7, and nonideal flow patterns in Chapter 8. In Chapter 8 we will return to the issue of detailed modeling of chemical reactors, which include all these effects. [Pg.181]

An integrated circuit is a multilayer, three-dimensional structure of electrically interconnected solid-state circuit elements isolated with patterned dielectric films. The dielectric, conductor, and semiconductor films are deposited or formed by sophisticated chemical reactions. The successful growth and manipulation of these films depend heavily on the proper design of chemical reactors used in deposition and etching, the choice of appropriate chemical reagents, separation and ultrapurification, and operation of sophisticated control systems. [Pg.378]

Below we discuss a particular case of coexisting stable front waves and calculate two-parameter bifurcation diagrams determining wave velocity vs. physical parameter relations. These results are then related to spatiotemporal patterns obtained by directly solving the partial differential equations which describe a bounded system. This system gives rise to an alternating pattern of fronts moving back and forth in the reactor. At the boundaries one type of front is transformed into the other one and is reflected back to the reactor. Such a pattern exists for the reaction-diffusion system (with Neumann boundary conditions) as well as for the reaction-diffusion-convection system (with Danckwerts boundary conditions). Observed zig-zag dynamics is both of theoretical and practical interest for operation of chemical reactors. [Pg.726]

Inputs from WWTP effluents can also affect the hydrologic and nutrient concentration regimes of recipient streams at different temporal scales. Daily variations of these parameters may be exacerbated in streams below the WWTP input by the diel patterns of the effluent discharge associated with plant operation [46]. In contrast, at the annual scale, seasonal variations of physical and chemical parameters upstream of the WWTP may be dampened by the constant input of additional water and nutrients from the WWTP. At its extreme, naturally intermittent or ephemeral streams may turn into permanent streams downstream of WWTPs [28, 30]. In these effluent-dominated streams, the relative contribution of WWTP inputs may vary widely on an annual basis, as shown by the 3-100% range measured in a Mediterranean stream [47]. Finally, WWTP inputs also cause shifts in the relative availability of N and P as well as in the relative importance of reduced and oxidized forms of N in the stream [30, 47]. The magnitude of these shifts depends on the level of wastewater treatment (i.e., primary, secondary, or tertiary treatment), the type of WWTP infrastructure (e.g., activated sludge reactor. [Pg.178]

Contacting patterns for various combinations of high and low concentration of reactants in noncontinuous operations (batch reactors). (Adapted from Chemical Reaction Engineering, Second Edition, by O. Levenspiel. Copyright 1972. Reprinted by permission of John Wiley and Sons, Inc.)... [Pg.319]

Example 4.8 Chemical reactions and reacting flows The extension of the theory of linear nonequilibrium thermodynamics to nonlinear systems can describe systems far from equilibrium, such as open chemical reactions. Some chemical reactions may include multiple stationary states, periodic and nonperiodic oscillations, chemical waves, and spatial patterns. The determination of entropy of stationary states in a continuously stirred tank reactor may provide insight into the thermodynamics of open nonlinear systems and the optimum operating conditions of multiphase combustion. These conditions may be achieved by minimizing entropy production and the lost available work, which may lead to the maximum net energy output per unit mass of the flow at the reactor exit. [Pg.174]

Owing mainly to their simple construction and the absence of moving parts and installments (which usually provide for a somewhat settled flow pattern) the hydro-dynamic behavior of BCR is rather complex and changes considerably with variations in physico-chemical properties and operational conditions. This causes difficulties in the design and scale-up of BCR and leads to errors and unreliabilities which, in turn, often result in overdimensioning of the reactors. [Pg.213]

Trade-offs in performance advantages between the honeycomb multichannel supports and others that offer variable flow patterns are necessary for each application. More compact and efficient reactors will provide many novel opportunities not only to improve chemical processes in wide industrial practice, but to develop novel processes for more efficient operation in the near future. [Pg.206]


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