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First order reversible

Without assuming something specific about the reaction rate, it is not possible to go further and actually determine the micropore fluxes. We shall therefore consider the particular case of a first order reversible isomeri-... [Pg.82]

Examples of first-order reversible reaetions are gas phase eis-trans isomerization, isomerizations in various types of hydroearbon systems, and the raeemization of a and (3 glueoses. An example of a eatalytie reaetion is the ortho-para hydrogen eonversion on a niekel eatalyst. [Pg.150]

Consider the first order reversible reaetion of the form... [Pg.317]

Fig ure 6-28. Rate of reaotion profile for a first order reversible reaetion A R. [Pg.522]

Consider a first order reversible reaetion A R, where the rate expression is (-r ) = - EjCr. Therefore, oti = = Dr = 1. Eor... [Pg.533]

Optimum temperature progression for a first order reversible reaction A o R... [Pg.534]

Also for polyethylene, by increasing the temperature, a first-order reversible transition can occur from the usual orthorhombic form toward a hexagonal disordered form, but only for sufficiently high values of the pressure (above 4 kbar) [70-73, 5],... [Pg.202]

This has been identified as the endo isomer, i.e. the one in which the Ce methyl group is inside (Koptyug et al., 1969). As in the case of 19, when 22 is warmed to — 34°, a clean first-order reversion to the hexa-... [Pg.134]

Determine a i) for a first-order, reversible reaction, A reactor. [Pg.31]

More complicated reactions schemes, including first-order reversible consecutive processes and competitive consecutive reactions, are considered in a textbook by Irwin [89]. Professor Irwin s textbook also includes computer programs written in the BASIC language. These programs can be used to fit data to the models described. [Pg.157]

P4.04.07. FIRST ORDER REVERSIBLE REACTION. UNSTEADY AND STEADY. [Pg.316]

The first order reversible reaction, A B, is carried out in a CSTR,... [Pg.316]

A stirred tank reactor with a pump-around heat exchanger is arranged as on the sketch. The first order reversible reaction, A B, is to be carried to 80% conversion. The reaction temperature is to be kept at the value at which equilibrium conversion would be 90%. Temperature drop across the exchanger is to 60 K. Reaction in the exchanger circuit is neglected. Operating data are shown on the sketch and other data are k = exp(17.2-5800/T), 1/hr... [Pg.346]

A first order reversible reaction, A B, is carried out in a plug flow reactor, starting with pure A. The specific rate and equilibrium constants are functions of temperature, k = A exp (-E/T)... [Pg.368]

Figure 7.5 CO conversion for the WGS reaction over G-66 A, Cu02Ce08O2 y and Cu01Ce09O2 y catalysts. The solid lines are model fits assuming first-order reversible kinetics. The dotted line represents equilibrium conversion for the specific feed gas composition. (Reprinted from [51]. With permission from Elsevier.)... Figure 7.5 CO conversion for the WGS reaction over G-66 A, Cu02Ce08O2 y and Cu01Ce09O2 y catalysts. The solid lines are model fits assuming first-order reversible kinetics. The dotted line represents equilibrium conversion for the specific feed gas composition. (Reprinted from [51]. With permission from Elsevier.)...
Increased conversion and product purity are not the only benefits of simultaneous separation during the reaction. The chromatographic reactor was also found to be a very suitable tool for studying kinetics and mechanisms of chemical and biochemical reactions. Some recent publications describe the results on investigation of autocatalytic reactions [135], first-order reversible reactions [136], and estimation of enantioselectivity [137,138]. It is beyond the scope of this chapter to discuss the details, but the interested reader is referred to an overview published by Jeng and Langer [139]. [Pg.185]

Another study was performed on a catalytic hydrogenation of 1,3,5-trimethyl-benzene to 1,3,4-trimethylcyclohexane, which is a typical first-order reversible reaction [168]. By optimizing various operating conditions it was possible to achieve a product purity of 96% and a reactant conversion of 0.83 compared to a thermodynamic equilibrium conversion of only 0.4. The results were successfully described with a mathematical model derived by the same authors [169]. Comparison to a real countercurrent moving bed chromatographic reactor yielded very similar results for both types [170]. [Pg.196]

First-order reversible chemical reaction following a reversible electron transfer. The ErCr mechanism can be written as ... [Pg.74]

First-Order Reversible Reactions. Though no reaction ever goes to completion, we can consider many reactions to be essentially irreversible because of the large value of the equilibrium constant. These are the situations we have examined up to this point. Let us now consider reactions for which complete conversion cannot be assumed. The simplest case is the opposed unimolecular-type reaction... [Pg.56]

First-order reversible reaction, A rR, Cro/C o = M, kinetics approximated or fitted by -rA = k Cp - k2C with an observed equilibrium conversion any constant 8, ... [Pg.103]

In very dilute cumene-air mixtures the kinetics are essentially first-order reversible with respect to cumene with an equilibrium conversion of 94%. [Pg.471]


See other pages where First order reversible is mentioned: [Pg.170]    [Pg.697]    [Pg.146]    [Pg.149]    [Pg.371]    [Pg.403]    [Pg.342]    [Pg.282]    [Pg.456]    [Pg.65]    [Pg.119]    [Pg.234]    [Pg.14]    [Pg.218]    [Pg.75]    [Pg.126]    [Pg.78]    [Pg.389]    [Pg.182]    [Pg.199]   
See also in sourсe #XX -- [ Pg.412 ]




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