Use the integral method to determine the reaction order for the di-tert-butyl peroxide decomposition described in Example 5-1.SolutionRecalling Example 5-1, the combined mole balance and rate law for a constant-volume batch reactor can be expressed in the form |
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(E5-1.5) | |
As a first guess we might try zero order, = 0, for which equation (ES-1.5) becomes |
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(CDE5-1.1) | |
| Integrating gives us | ||
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Assuming a zero-order reaction |
If this is the correct order, a plot of PTversus t should be linear. After using the data in Table CDE5-1.1 to obtain Figure CDE5-1.1, we see that PT is not a linear function of t. Consequently, we conclude that the reaction is not zero-order. | |
![]() Figure CDE5-1-1 |
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Next we try second order, = 2: |
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| Integrating yields | ||
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| Assuming a second-order reaction | If the reaction is second order, a plot of versus t should be linear:![]() |
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After forming Table CDE5-1.1, a plot of versus t was constructed and is shown in Figure CDE5-1.2. From the curvature of the plot, we conclude that the reaction is not second order. |
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Finally, we try first order (i.e. = 1). If zero, first, or second order do not seems to describe the reaction rate equation, it is usually best to try some other method of determining the reaction order. for = 1, |
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Integrating with limits, when t = 0 yields |
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If the reaction is first order, a plot of versus t should be linear. After completing Table CDE5-1.2 using the raw data, a plot of as a function of time is made using semilog paper as shown in Figure CDE5-1.3. From the plot we see that is indeed linear with time, and we therefore conclude that the decomposition of di-tert-butyl peroxide follows first-order kinetics. From the slope of the plot in Figure CDE5-1.3, we can determine the specific reaction rate, k = 0.08 min -1 |
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![]() Figure CDE5-1.3 |