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Reaction rates reactant concentration

The mathematical relationship between reaction rate and concentration of reactant(s) is the rate law. For this simple case, the rate law is... [Pg.431]

The dependence of reaction rate on concentration is readily explained. Ordinarily, reactions occur as the result of collisions between reactant molecules. The higher the concentration of molecules, the greater the number of collisions in unit time and hence the faster the reaction. As reactants are consumed, their concentrations drop, collisions occur less frequently, and reaction rate decreases. This explains the common observation that reaction rate drops off with time, eventually going to zero when the limiting reactant is consumed. [Pg.288]

Kinetic results such as those presented in the previous sections, which could be further extended by varying the reaction parameters (reactant concentration, electrode potential, catalyst loading, electrolyte flow rate, and reaction temperature), can serve as basis... [Pg.450]

The diffusion model assumes that (1) Fick s law is valid as modified by reactions (2) reactant concentrations are interpreted as probability densities (3) specific rates correspond to otherwise homogeneous reactions—Monchick et al. (1957) show that this implies neglect of interparticle correlation, which is... [Pg.199]

Another factor that affects the rate of a chemical reaction is the concentration of reactants. As noted, most reactions take place in solutions. It is expected that as the concentration of reactants increases more collisions occur. Therefore, increasing the concentrations of one or more reactants generally leads to an increase in reaction rate. The dependence of reaction rate on concentration of a reactant is determined experimentally. A series of experiments is usually conducted in which the concentration of one reactant is changed while the other reactant is held constant. By noting how fast the reaction takes place with different concentrations of a reactant, it is often possible to derive an expression relating reaction rate to concentration. This expression is known as the rate law for the reaction. [Pg.143]

At high rates of reaction, the reactant concentration in the center of the specimen, Co, approaches zero closely. [Pg.183]

The simplest reactions have the one-step unimolecular or bimolecular mechanisms illustrated in Table 4.1 along with their differential rate equations, i.e. the relationships between instantaneous reaction rates and concentrations of reactants. That simple unimolecular reactions are first order, and bimolecular ones second order, we take as self-evident. The integrated rate equations, which describe the concentration-time profiles for reactants, are also given in Table 4.1. In such simple reactions, the order of the reaction coincides with the molecularity and the stoichiometric coefficient. [Pg.80]

Fundamentals - Effect of Concentration. The simplest relation between reaction rate and concentrations of the reactants is a power law. For the reaction... [Pg.30]

In principle, the steady-state rate expression for any enzyme with any number of reactants can be derived using the methods of the previous section. In practice, the procedure is very laborious, so use is made of an algorithmic method, introduced by King and Altman in 1956 it is not applicable to (1) nonenzymatic reactions (each reactant concentration must be S>[E]0), (2) mixtures of enzymes, or (3) reactions with nonenzymatic steps. However, these are not severe restrictions. It is applied as follows ... [Pg.257]

Our landmark value for a reasonable reaction rate at room temperature is highly dependent on AG, the molecularity of the reaction, the reactant concentrations, and on... [Pg.48]

The plug flow reactor is probably the most commonly used reactor in catalyst evaluation because it is simply a tube filled with catalyst that reactants are fed into. However, for catalyst evaluation, it is difficult to measure the reaction rate because concentration changes along the axis, and there are frequently temperature gradients, too. Furthermore, because the fluid velocity next to the catalyst is low, the chance for mass transfer limitations through the film around the catalyst is high. Eq. (3) is the reactor performance equation for a plug flow reactor. [Pg.2560]

Fig. 1 Monotonic and non-monotonic dependence of the rate of reaction on reactant concentrations. Fig. 1 Monotonic and non-monotonic dependence of the rate of reaction on reactant concentrations.
The negative effective reaction order with respect to steam, which is observed for the least acidic support, very strongly suggests a non-monotonic dependence of the rate of reaction upon reactant concentration, thus type 11 mechanism [5] is most probable with competition between steam and methane for the same active sites with positive order in certain regions and negative order in the other regions. [Pg.87]

The relations (27) and (28) are valid for very fast reactions with reactant concentrations at the surface near zero. Villermaux [90] proposed a correction function for surface reactions with lower rates. [Pg.70]

Concentration molecules must collide to react. A major factor influencing the rate of a given reaction is reactant concentration. A reaction can occur only when the reactant molecules collide. The more molecules present in the... [Pg.499]

With the rate, reactant concentrations, and reaction orders known, the sole remaining unknown in the rate law is the rate constant, k. The rate constant is specific for a particular reaction at a particular temperature. The experiments with the reaction of O2 and NO were run at the same temperature, so we can use data from any to solve for k. From experiment I in Table 16.2, for instance, we obtain... [Pg.509]

Figure 8.29 Reaction rate versus concentration of iimitmg reactant rate expression is neither convex nor concave. Figure 8.29 Reaction rate versus concentration of iimitmg reactant rate expression is neither convex nor concave.
Increasing the concentration of reactants increases the chances of collisions between reactant molecules. In other words, increasing concentration increases the number of collisions between molecules per second. This increases the reaction rate. The concentration of a gas increases with its partial pressure. So, we can increase the rate of gaseous reactions by increasing the partial pressure of the reactants. [Pg.246]

And is called kinetic equation or reaction rate law. Here r. is rate of reactions normalized over volume, C.,. is molar concentrations of reac-tants, k. is constant value characterizing the rate reactions at reactants concentration equal to 1, which is called reaction rate constant or intrinsic reaction rate, v.. is stoichiometric coefficient of the component i usually called partial order of reaction. Sum of one reaction partial order determines order of the reaction overall or order of its rate law. Elementary reactions (acts) dominate, which are subject to the rate law of zero, first and second order. For instance, for an elementary direct reaction... [Pg.67]

The recommendations to measure the inter micellar dynamics are (1) to use a fast reaction with reactant concentration such that only single-ion occupation appears and (2) to choose the droplet concentration of the microemulsion low enough to be in a diffusion-controlled state. Therefore, experiments were carried out in low surfactant concentration samples at low R values with single-ion occupation for the droplets. The reactants were solubilized in freshly prepared microemulsions of the same composition. For all the rate measurements the pseudo-first-order conditions were applied so that the metal ion concentration exceeded the murexide concentration by a factor of 10. [Pg.525]

Basically, a fuel cell electrode can, thus, be seen as a highly dispersed interface between Pt and electrolyte (ionoiner or water). Due to the random composition, complex spatial distributions of electrode potential, reaction rates, and concentrations of reactants and water evolve under PEMFC operation. A subtle electrode theory has to establish the links between these distributions. [Pg.46]

It is important to investigate the effects on the reaction kinetics and rates of heat generation and gas evolution of factors such as scale-up, agitator configuration, materials of construction, variations in addition rate, reactant concentration and hold times. The effects of process maloperations should also be established. [Pg.33]

Determination of a singie species Pseudo-first-order reactions Initial rate method Fixed-time method Variable-time method Second-order reactions Identical reactant concentrations Unequal reactant concentrations Multipoint methods Curve-fitting methods Predictive methods Error-compensated methods... [Pg.2416]

The integrated rate law for a first-order reaction is = Cj e, where is the concentration of reactant species A at time t and is the initial concentration of reactant species A at time t = 0. For a first-order reaction, the reactant concentration decreases exponentially with time. The rate constant k for a first-order reaction has units of time ... [Pg.79]

The rate equation for a chemical reaction is an equation that links the reaction rate with concentrations of reactants and the rate coefficient Take a simple chemistry equation as an example ... [Pg.434]

Although the above simple illustration of the concept for a homogeneous isothermal lumped system is applicable to other more complicated systems, the situation for catalytic reactors is much more involved because of the complexity of the intrinsic kinetics as well as the complex interaction among reactions, heat release (or absorption), and mass and heat diffusion inside the reactor. For example, many catalytic and biocatalytic reactions show nonmonotonic dependence of the rate of reaction on reactant concentrations. For example, the hydrogenation of benzene to cyclohexane over different types of nickel catalyst has an intrinsic rate of reaction of the form... [Pg.217]


See other pages where Reaction rates reactant concentration is mentioned: [Pg.98]    [Pg.159]    [Pg.28]    [Pg.364]    [Pg.617]    [Pg.88]    [Pg.193]    [Pg.445]    [Pg.434]    [Pg.630]    [Pg.623]    [Pg.542]    [Pg.985]    [Pg.159]    [Pg.1027]    [Pg.88]    [Pg.100]    [Pg.33]    [Pg.79]    [Pg.161]    [Pg.237]   
See also in sourсe #XX -- [ Pg.278 ]




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