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Reactant identity

A parallel reactor system has an extra degree of freedom compared with a series system. The total volume and flow rate can be arbitrarily divided between the parallel elements. For reactors in series, only the volume can be divided since the two reactors must operate at the same flow rate. Despite this extra variable, there are no performance advantages compared with a single reactor that has the same total V and Q, provided the parallel reactors are at the same temperature. When significant amounts of heat must be transferred to or from the reactants, identical small reactors in parallel may be preferred because the desired operating temperature is easier to achieve. [Pg.135]

Fig. 14.24. The Marcus theory is based on two parabolic diabatic potentials (9) and V/> ( ) for the reactants (gray curve) and products (black curve), having minima at and <]p, respectively. The quantity AG = Vp(qp) — Vp(qp) represents the energy differencebetweentheproductsandthereactantsattheirequilibriumgeometries, the reaction barrier AG = Vp qc) — Vp(qp) = Vp(qc), where 5c corresponds to the intersection of the parabolas. The reotgarrization energy A = Vp qp) — Vp qp) = Vp(qp) represents the energy expense for makirrg the geometry of the reactants identical with that of the products (and vice versa). Fig. 14.24. The Marcus theory is based on two parabolic diabatic potentials (9) and V/> ( ) for the reactants (gray curve) and products (black curve), having minima at and <]p, respectively. The quantity AG = Vp(qp) — Vp(qp) represents the energy differencebetweentheproductsandthereactantsattheirequilibriumgeometries, the reaction barrier AG = Vp qc) — Vp(qp) = Vp(qc), where 5c corresponds to the intersection of the parabolas. The reotgarrization energy A = Vp qp) — Vp qp) = Vp(qp) represents the energy expense for makirrg the geometry of the reactants identical with that of the products (and vice versa).
The fact that the steady-state rate constant k differs from the equilibrium rate constant /fgq illustrates an interesting notion due to Ross and Mazur,viz., that a rate constant is affinity-dependent. From this point of view, since k characterizes a system in which reaction products are instantaneously removed, it is the rate constant at infinite affinity, and since xeq characterizes a system in which products and reactants are in equilibrium, it is the rate constant at zero affinity. Suppose a reaction system is prepared with all the A molecules initially in reactant states but with product molecules allowed to accumulate. Presumably in the initial relaxation period there will be established a distribution of reactants identical to that found when products are instantaneously removed, and the reaction will then proceed with a rate constant x but as products gradually accumulate the reactant distribution will gradually approach the equilibrium distribution, and the rate constant will gradually (and, as seems likely, mono-tonically) approach >ceq. Thus, whether the reaction proceeds the whole way from initiation to completion with a single rate constcint or with a varying rate constant depends entirely on whether there is a measurable difference between k and xgq. [Pg.381]

Reactive scattering or a chemical reaction is characterized by a rearrangement of the component particles within the collision system, thereby resulting in a change of the physical and chemical identity of the original collision reactants A + B into different collision products C + D. Total mass is conserved. The reaction is exothemiic when rel(CD) > (AB) and is endothermic when rel(CD) < (AB). A threshold energy is required for the endothemiic reaction. [Pg.2007]

Catalysis in a single fluid phase (liquid, gas or supercritical fluid) is called homogeneous catalysis because the phase in which it occurs is relatively unifonn or homogeneous. The catalyst may be molecular or ionic. Catalysis at an interface (usually a solid surface) is called heterogeneous catalysis, an implication of this tenn is that more than one phase is present in the reactor, and the reactants are usually concentrated in a fluid phase in contact with the catalyst, e.g., a gas in contact with a solid. Most catalysts used in the largest teclmological processes are solids. The tenn catalytic site (or active site) describes the groups on the surface to which reactants bond for catalysis to occur the identities of the catalytic sites are often unknown because most solid surfaces are nonunifonn in stmcture and composition and difficult to characterize well, and the active sites often constitute a small minority of the surface sites. [Pg.2697]

Resonance stabilization energies are generally assessed from thermodynamic data. If we define to be the resonance stabilization energy of species i, then the heat of formation of that species will be less by an amount ej than for an otherwise equivalent molecule without resonance. Likewise, the AH for a reaction which is influenced by resonance effects is less by an amount Ae (A is the usual difference products minus reactants) than the AH for a reaction which is otherwise identical except for resonance effects ... [Pg.440]

Related to the preceding is the classification with respect to oidei. In the power law rate equation / = /cC C, the exponent to which any particular reactant concentration is raised is called the order p or q with respect to that substance, and the sum of the exponents p + q is the order of the reaction. At times the order is identical with the molecularity, but there are many reactions with experimental orders of zero or fractions or negative numbers. Complex reactions may not conform to any power law. Thus, there are reactions of ... [Pg.683]

The checkers preferred o -methylnaphthalene (Eastman, Practical) as the diluent. When it is used in the apparatus described the phenol does not distil, so that a reaction flask fitted with an air-cooled condenser is more convenient. The reactants in 60 g. of -methylnaphthalene are heated in an oil bath at 230° for 1.5 to 2 hours. Three grains of Norite and 20 g. more of a-methylnaphthalene are then added, and the mixture is treated as described in the Procedure. The yield and melting point of the product are identical with those described. [Pg.93]

The role that acid and base catalysts play can be quantitatively studied by kinetic techniques. It is possible to recognize several distinct types of catalysis by acids and bases. The term specie acid catalysis is used when the reaction rate is dependent on the equilibrium for protonation of the reactant. This type of catalysis is independent of the concentration and specific structure of the various proton donors present in solution. Specific acid catalysis is governed by the hydrogen-ion concentration (pH) of the solution. For example, for a series of reactions in an aqueous buffer system, flie rate of flie reaction would be a fimetion of the pH, but not of the concentration or identity of the acidic and basic components of the buffer. The kinetic expression for any such reaction will include a term for hydrogen-ion concentration, [H+]. The term general acid catalysis is used when the nature and concentration of proton donors present in solution affect the reaction rate. The kinetic expression for such a reaction will include a term for each of the potential proton donors that acts as a catalyst. The terms specific base catalysis and general base catalysis apply in the same way to base-catalyzed reactions. [Pg.229]

The details of proton-transfer processes can also be probed by examination of solvent isotope effects, for example, by comparing the rates of a reaction in H2O versus D2O. The solvent isotope effect can be either normal or inverse, depending on the nature of the proton-transfer process in the reaction mechanism. D3O+ is a stronger acid than H3O+. As a result, reactants in D2O solution are somewhat more extensively protonated than in H2O at identical acid concentration. A reaction that involves a rapid equilibrium protonation will proceed faster in D2O than in H2O because of the higher concentration of the protonated reactant. On the other hand, if proton transfer is part of the rate-determining step, the reaction will be faster in H2O than in D2O because of the normal primary kinetic isotope effect of the type considered in Section 4.5. [Pg.232]

Allyl esters undergo rearrangement reactions at 300°C and above. Two examples are shown, one of which is degenerate, since the product and reactant are identical ... [Pg.260]

Attack by a nucleophile or the solvent can occur at either of the ion pairs. Nucleophilic attack on the intimate ion pair would be expected to occur with inversion of configuration, since the leaving group would still shield the fiont side of the caibocation. At the solvent-separated ion pair stage, the nucleophile might approach fiom either fece, particularly in the case where solvent is the nucleophile. Reactions through dissociated carbocations should occur with complete lacemization. According to this interpretation, the identity and stereochemistry of the reaction products will be determined by the extent to which reaction occurs on the un-ionized reactant, the intimate ion pair, the solvent-separated ion pair, or the dissociated caibocation. [Pg.270]

A more difficult criterion to meet with flow markers is that the polymer samples not contain interferents that coelute with or very near the flow marker and either affect its retention time or the ability of the analyst to reproducibly identify the retention time of the peak. Water is a ubiquitous problem in nonaqueous GPC and, when using a refractive index detector, it can cause a variable magnitude, negative area peak that may coelute with certain choices of totally permeated flow markers. This variable area negative peak may alter the apparent position of the flow marker when the flow rate has actually been invariant, thereby causing the user to falsely adjust data to compensate for the flow error. Similar problems can occur with the elution of positive peaks that are not exactly identical in elution to the totally permeated flow marker. Species that often contribute to these problems are residual monomer, reactants, surfactants, by-products, or buffers from the synthesis of the polymer. [Pg.549]

In Scheme Vll the reactants A and B compete for reagent R. There may be additional products the essence of the description is that the analytical method responds identically to the products of the two reactions. [Pg.64]

Let us now turn to the surfaces themselves to learn the kinds of kinetic information they contain. First observe that the potential energy surface of Fig. 5-2 is drawn to be symmetrical about the 45° diagonal. This is the type of surface to be expected for a symmetrical reaction like H -I- H2 = H2 -h H, in which the reactants and products are identical. The corresponding reaction coordinate diagram in Fig. 5-3, therefore, shows the reactants and products having the same stability (energy) and the transition state appearing at precisely the midpoint of the reaction coordinate. [Pg.197]

The ortho effect may consist of several components. The normal electronic effect may receive contributions from inductive and resonance factors, just as with tneta and para substituents. There may also be a proximity or field electronic effect that operates directly between the substituent and the reaction site. In addition there may exist a true steric effect, as a result of the space-filling nature of the substituent (itself ultimately an electronic effect). Finally it is possible that non-covalent interactions, such as hydrogen bonding or charge transfer, may take place. The role of the solvent in both the initial state and the transition state may be different in the presence of ortho substitution. Many attempts have been made to separate these several effects. For example. Farthing and Nam defined an ortho substituent constant in the usual way by = log (K/K ) for the ionization of benzoic acids, postulating that includes both electronic and steric components. They assumed that the electronic portion of the ortho effect is identical to the para effect, writing CTe = o-p, and that the steric component is equal to the difference between the total effect and the electronic effect, or cts = cr — cte- They then used a multiple LFER to correlate data for orrAo-substituted reactants. [Pg.336]

An isodesmic reaction is one in which the total number of each type of bond is identical in the reactants and products. Here is a simple example ... [Pg.181]

Figure 14.12 The TS for an identity S at2 reaction has a higher symmetry than the reactant/ product... Figure 14.12 The TS for an identity S at2 reaction has a higher symmetry than the reactant/ product...
The [l,5]-hydrogen shift in Z-l,3-pentadiene is an example of a narcissistic reaction, with the reactant and product being identical. The TS is therefore located exactly at half-way, and has a symmetry different from either the reactant or product. By suitable constraints on the geometry the TS may therefore be located by a minimization within a symmetry consti ained geometry. [Pg.420]

In an alkaline medium the condensation of carbonyl and amino groups of the reactants seems to be more probable (pathway 1), although pathway 2, which is identical to the reactions of enaminoketones, is also possible. [Pg.223]

The precipitation reaction that occurs when solutions of Na2C03 and CaCl2 are mixed (Figure 4.5) can be represented by a simple equation. To obtain that equation, consider the identity of the reactants and products ... [Pg.79]

In earlier sections of this chapter, we showed how to write and balance equations for precipitation reactions (Section 4.2) and acid-base reactions (Section 4.3). In this section we will concentrate on balancing redox equations, given the identity of reactants and products. To do that, it is convenient to introduce a new concept, oxidation number. [Pg.87]


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