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Order of reaction, calculation

Find the order of reaction. Calculate rate constant and the rate of decomposition of A, when [A] = 0.45 mol dm 3. [Pg.15]

The effect of substrate concentration on the rate of oxidation was determined in the range of 5.94 x 10 to 23.00 x 10 mol 1 at 35°C and 1 atm. pressure at a constant catalyst concentration of 3.22 X 10 mol 1 ofRu(III) for catalyst B and 1.55 x 1 O mol f ofRu (III) for catalyst F. It was observed that the rate of oxidation increases linearly with respect to substrate concentration. The order of reaction calculated from the linear plots of log (initial rate) vs. log [cyclohexene] was found to be fractional for both catalysts. [Pg.1170]

The reaction was carried out by varying the concentration of toluene from 4.70 x 10 M to 18.8 X 10 M at 35 C and 1 atm O2 pressure using a fixed amount of the catalyst i.e. 6.25 X 1 O g of Pd present on the surface. The rate was found to increase with an increase in the concentration of toluene (Table 3). The order of reaction calculated from the slope of the linear plot of log (initial rate) Vs log [toluene] was found to be 0.357 which is indicative of the fractional order. [Pg.295]

Fig. 4a-b. Total relative activity of enzyme membranes calculated for different cf values in function of the normalized external substrate concentration (number of Si Km) in symmetrical systems (a) with first order reaction (from Goldman et al. [53]) (see Table IV), (b) with no assumption on the order of reaction (calculated by Selegny and Leguillon using 5 term Mac Laurin series of Table VI). [Pg.444]

Dioxetanones decompose near or below room temperature to aldehydes or ketones (56). The decomposition reactions are weakly chemiluminescent Qc ca 10 ein/mol) because the products are poorly fluorescent. However, addition of 10 M mbrene provides 2iQc ca 10 ein/mol, and 2iQc on the order of was calculated at mbrene concentrations above 10 M after correcting for yield loss factors (57). The decomposition rates are first order ia... [Pg.266]

The orders of reaction, U , ivith respect to A, B and AB are obtained from the rate expression by differentiation as in Eq. (11). In the rare case that we have a complete numerical solution of the kinetics, as explained in Section 2.10.3, we can find the reaction orders numerically. Here we assume that the quasi-equilibrium approximation is valid, ivhich enables us to derive an analytical expression for the rate as in Eq. (161) and to calculate the reaction orders as ... [Pg.63]

Stating all assumptions made, calculate EA, the Arrhenius energy of activatioa for the reaction. Note that the order of reaction is not known. [Pg.62]

From these results, determine the order of reaction, and calculate the value of the rate constant in pressure units (kPa) and in concentration units (mol L-1). [Pg.72]

The presence (or absence) of pore-diffusion resistance in catalyst particles can be readily determined by evaluation of the Thiele modulus and subsequently the effectiveness factor, if the intrinsic kinetics of the surface reaction are known. When the intrinsic rate law is not known completely, so that the Thiele modulus cannot be calculated, there are two methods available. One method is based upon measurement of the rate for differing particle sizes and does not require any knowledge of the kinetics. The other method requires only a single measurement of rate for a particle size of interest, but requires knowledge of the order of reaction. We describe these in turn. [Pg.208]

Taking the order of reaction to be exactly 2, although there is no absolute necessity for the order to be an integer, the rate constants for each of the runs, 1 and 2, may now be calculated. [Pg.267]

As far as the second part of the supposition 2 is concerned, namely that initiation is by addition of an A1X2 ion to the monomer (reaction (8)), there is as yet no direct evidence for it moreover, such evidence is very difficult to obtain. The problem is that of identifying a C-Al bond in concentrations which are likely to be in the micro-molar range. An approximate order-of-magnitude calculation may illustrate the difficulty of the task. [Pg.274]

If the concentration of a reactant changes and that has no effect on the rate of reaction, then the reaction is zero-order with respect to that reactant ([2]° = 1). Many times, we calculate the overall order of reaction it is simply the sum of the individual coefficients, third order in this example. [Pg.190]

Once the rate has been determined, the orders of reaction can be determined by conducting a series of reactions in which we change the concentrations of the reactant species one at a time. We then mathematically determine the effect on the reaction rate. Once the orders of reaction have been determined, we calculate the rate constant. [Pg.190]

Kinetics is the study of the speed of reactions. The speed of reaction is affected by the nature of the reactants, the temperature, the concentration of reactants, the physical state of the reactants, and catalysts. A rate law relates the speed of reaction to the reactant concentrations and the orders of reaction. Integrated rate laws relate the rate of reaction to a change in reactant or product concentration over time. We may use the Arrhenius equation to calculate the activation... [Pg.200]

In this method, the different rate equations in their integrated forms (given in Table 1) are used. The amount of reactant a - x or product x at different time intervals t is first experimentally determined. Then the values of x, a-x and time are introduced into the different rate equations and the value of rate constant k is calculated at different time intervals. The equation which gives the constant value of rate constant indicates the order of reaction. For example, the values of rate constants at different time intervals are same in equation... [Pg.30]

The optical density of samples are measured at different times using same cell (to keep l constant) and concentration can be calculated using relation c = AlEl. To verify the order of reaction, optical density data can be used directly. [Pg.44]

Thus, the measurement of and cf at a given flow rate u allows the reaction rate to be calculated from equation (7.7). The order of reaction and rate constant can be determined by carrying out experiments at different concentrations of reactants and rates of flow. [Pg.177]

In this expression, k is the rate constant—a constant for each chemical reaction at a given temperature. The exponents m and n, called the orders of reaction, indicate what effect a change in concentration of that reactant species will have on the reaction rate. Say, for example, m = 1 and n = 2. That means that if the concentration of reactant A is doubled, then the rate will also double ([2]1 = 2), and if the concentration of reactant B is doubled, then the rate will increase fourfold ([2]2 = 4). We say that it is first order with respect to A and second order with respect to B. If the concentration of a reactant is doubled and that has no effect on the rate of reaction, then the reaction is zero order with respect to that reactant ([2]° = 1). Many times the overall order of reaction is calculated it is simply the sum of the individual coefficients, third order in this example. The rate equation would then be shown as ... [Pg.199]

At any radius r, the rate of reaction per unit area can be calculated from the quotient, (dn/dt)r/Sr. Consequently, the specific rate of reaction and calculated carbon dioxide concentration (both taken at the same value of r) can be plotted to determine the true order of reaction, independent of diffusion control. Figure 19 presents such data for the carbon rod reacted at 1200°, assuming the relative concentrations for Case 3 in Table VI to be applicable. From an auxiliary plot similar to Fig. 19, a finite reaction rate at zero carbon dioxide concentration is found. Since the concentrations of carbon dioxide were calculated assuming Co to be zero, it is clear that this reaction rate is due to a finite Co concentration at the center of the rod. The actual values of concentration at values of r were estimated by extrapolat-... [Pg.193]

For n t- 1 it is important to keep in mind that the half-life is a function of the initial concentration c(A)a. Knowing the order of reaction and the rate constant allows the half-life to be calculated. Or it can be determined experimentally and used to calculate the other parameters, e. g. by the trial and error method. [Pg.111]

Edward Koubeck, "An Experiment To Demonstrate How a Catalyst Affects the Rate of a Reaction," /. Chem. Educ., Vol. 76,1999, 1714-1715. Describes a chemistry experiment that allows students to calculate rates of reaction, orders of reaction, and activation energies. [Pg.509]

So, in this method, we start with two different concentrations of the reactants and note the time for the completion of any fraction, say, half change in each case. By substituting these values in the last equation, we can calculate the order of reaction, n. [Pg.229]

Order of reaction (n) can be calculated by half change method by the following formula ... [Pg.240]

Calculate the specific reaction rate and order of reaction. Sol. Diazobenzene chloride deomposes as ... [Pg.242]


See other pages where Order of reaction, calculation is mentioned: [Pg.1170]    [Pg.295]    [Pg.1170]    [Pg.295]    [Pg.393]    [Pg.1045]    [Pg.113]    [Pg.419]    [Pg.93]    [Pg.319]    [Pg.81]    [Pg.169]    [Pg.277]    [Pg.169]    [Pg.257]    [Pg.101]    [Pg.174]    [Pg.238]    [Pg.55]    [Pg.1089]    [Pg.245]    [Pg.246]    [Pg.247]    [Pg.58]    [Pg.73]    [Pg.59]   


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