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Reaction rates temperature effects

Concentration effect on reaction rate Temperature effect on reaction rate Surface area effect on reaction rate Chemical equilibrium conditions Simultaneous forward and reverse reaction Rate forward reaction = rate reverse reaction Reaction system is closed ... [Pg.358]

What effect does surface area have on reaction rate What effect does a combination of surface area and temperature have on reaction rate ... [Pg.133]

The higher reactivity of the PVMI-Co(III) complex is attributed to the electrostatic domain of the polymer complex, as in the above PVP system. When the PVMI chain contracts, the charge density in the polymer domain increases and the reaction rate also increases. On the other hand, when the polymer chain expands, the electrostatic domain is weakened, which produces a fall in reactivity. These results confirm that the conformation of the polymer complex is closely related to the strength of its electrostatic domain and to the reaction rate. The effects of the polymer chain on reactivity are to be understood not only in terms of static chemical environment but also as dynamic effects which vary with the solution conditions, e.g. pH, ionic strength, solvent composition, temperature, and so on. [Pg.45]

This methodology can be used for the calculation of local reaction rates and effectiveness factors in dependence on gas components concentrations, temperature and porous catalytic layer structure (cf. Fig. 9). The results can then be used as input values for simulations at a larger scale, e.g. the effective reaction rates averaged over the studied washcoat section can be employed as local reaction rates in the ID model of monolith channel. [Pg.122]

The overall effect of temperature on reaction rates is a combination of the effects produced at each stage. In general, a 10 °C increase in T will double the rate of an enzymatic reaction. Temperature control to within 0.1 °C is necessary to ensure the reproducible measurement of reaction rates. Temperatures <40 °C are generally employed, to avoid protein denaturation. [Pg.38]

Use of experimental data and graphical analysis to determine reactant order, rate constants, and reaction rate laws Effect of temperature change on rates Energy of activation the role of catalysts... [Pg.4]

In general, reaction rates are strongly dependent on the temperature when the activation energy is high. Thus it is assumed that the two major effects of the reaction rate, temperature and concentration of the reactant, tend to cancel each other ... [Pg.49]

According to the colhsion theory of reaction rates, the effect of temperature on the rate of a chemical reaction is defined by the Arrhenius equation ... [Pg.243]

Figure P12.17-2 Effect of pressure on the reaction rate. Temperature, 25 to 26°C hydrogen flow rate, 27.6 x 10" mol/s catalyst weight, 0.976 g stirrer speed, 1500 rpm. Figure P12.17-2 Effect of pressure on the reaction rate. Temperature, 25 to 26°C hydrogen flow rate, 27.6 x 10" mol/s catalyst weight, 0.976 g stirrer speed, 1500 rpm.
This is not a theoretical dependence of on temperature but is useful for the following discussions. At strong influence of internal diffusion on the reaction rate, the effectiveness factor was found to be inversely proportional to the Thiele modulus (e.g.. Equation 2.176). Accordingly, the effective rate constant is given by ... [Pg.81]

To produce geochemical rate models, rates determined by reactor experiments must be converted into rate equations that summarize how the rate varies with solution composition, temperature, and other rate-determining variables. If the rates are determined at near-equilibrium conditions, the rate data must be fit to an equation that takes into account both the forward and reverse rate. Most geochemical rate experiments are designed to measure rates for far-from-equilibrium conditions where the reverse reaction rate is effectively zero. These experimental rates can be fit to a simple equation that relates the rate to the product of the concentration (w, molal) of each reacting species raised to a power (n). [Pg.72]

It can be seen from equation (7.15) that the temperature difference is proportional to reaction rate, heat effect and the square of diameter of the reactor, and is inversely proportional to the effective conductivity factor. The temperature difference increases with a decrease in the particle diameter of catalysts because the effective conductivity factor A reduces with the decrease in the size of catalyst particles. When decreasing the particle diameter of catalyst in order to eliminate the effect of inside diffusion on reaction, it also enhances the factor of temperature difference. Therefore, it need to weigh the pros and cons of these factors in order to determine the most appropriate particle size of catalyst and the diameter of reactor. [Pg.558]

The interpretation of Equations 3.95 and 3.96, as well as Equations 3.97 and 3.98, is simple if the number of molecules in the chemical reaction increases, the expression attains a positive value (since > 0 and > 0). Simultaneously, the terms in parentheses, in Equations 3.95 through 3.98, become larger than unity (>1) inside the reactor. Under isothermal conditions (T = To), the volumetric flow rate inside the reactor is thus increased. Under nonisothermal conditions—with strongly exothermic or endothermic reactions— the temperature effect, that is, the term T/Tq, results in a considerable change in the volumetric flow rate. [Pg.57]

Equations (20A2) and f20.13i must be solved for a given rate expression to get the actual relationship between the indicated parameters. However, several generalizations are possible. The reactor volume and conversion change in the same direction. As one increases, so does the other as one decreases, so does the other. As the reaction rate increases, the volume required decreases, and vice versa. As the reaction rate increases, the conversion increases, and vice versa. It has already been discussed how temperature, pressure, and concentration affect the reaction rate. Their effect on conversion and reactor volume is derived from their effect on reaction rate. Example 20.2 illustrates these qualitative generalizations. [Pg.664]

This reaction occurs at hi pressure (810 MPa) in the presence of a catalyst, such as sodium methoxide, at low temperature (80°C) [87]. The effects of various alkali metal alkoxides has been investigated, and the activity of the catalyst has been shown to increase with increasing ionization potential of the metal [94]. From kinetic studies it has also been shown that both C02 and H2Q react with the catalyst, resulting in a reduced reaction rate. The effect of C02 is twice as severe as that of water [95],... [Pg.199]

A number of approaches have been suggested to cope with this (somewhat artificial) problem created by the cold boundary . Typical of these is the adaptation of the Arrhenius temperature dependence. It is generally the case that the reaction rate is effectively zero for temperatures up to some ignition temperature Ti > Tq. We can choose to work with a modified temperature dependence f 0) such that f 9) = 0 forO < 9 < 6i and f 0) = f 9) for 9i < 9 <. This introduces a discontinuity and a somewhat arbitrary new... [Pg.509]

The Effect of Reactant Concentration on Reaction Rates The Effect of Temperature on Reaction Rates The Effect of Catalysts on Reaction Rates... [Pg.1213]

The enhancement of the toluene steam dealkylation reaction is feasible by microwave irradiation (Litvishkov et al., 2012). It has been found that the most likely cause of the positive effect of microwave radiation on the reaction rate is an increase in the preexponential factor of the Arrhenius equation for the temperature dependence of the reaction rate. This effect is presumably due to an increase in the active surface area of the catalyst formed by the microwave-assisted thermal treatment. [Pg.113]

The most puzzling thing about the epinine data in Table XIII is that as the temperature is decreased the amount of hydroxylation reaction in the presence of ascorbate actually increases, i.e., there is a reverse-temperature effect. This result can be explained if one makes the further assumption that the postulated epinine-hydroperoxide intermediate is unstable at 35°C., so that the steady-state concentration of the intermediate is somewhat lower at 35°C. than at 22°C. The inverse temperature effect for dopamine hydroxylation, not seen in the 22°C. to 35°C. range, but apparent in the 35°C. to 49°C. range, could be explained in the same way if the dopamine-peroxide intermediate were relatively stable at 35°C. but unstable at 49°C. At that high temperature, however, enzyme inactivation may play a role. An additional factor which may contribute to these inverse rate-temperature effects is the decreased solubility of one of the substrates, oxygen, at higher temperatures. [Pg.177]


See other pages where Reaction rates temperature effects is mentioned: [Pg.1037]    [Pg.48]    [Pg.149]    [Pg.59]    [Pg.59]    [Pg.283]    [Pg.715]    [Pg.8]    [Pg.16]    [Pg.373]    [Pg.706]    [Pg.376]    [Pg.211]    [Pg.1440]    [Pg.218]    [Pg.150]    [Pg.47]    [Pg.843]    [Pg.856]    [Pg.1094]    [Pg.1351]    [Pg.2115]    [Pg.256]    [Pg.262]   
See also in sourсe #XX -- [ Pg.218 ]

See also in sourсe #XX -- [ Pg.88 ]

See also in sourсe #XX -- [ Pg.216 ]




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