Given that the rate of a first-order reaction is decreasing over time, we can use the integrated rate law for first-order kinetics:
Rate = \( k[A]_0 e^{-kt} \)
At time \( t = 10 \) min:
0.04 = \( k[A]_0 e^{-k \times 600} \)
At time \( t = 20 \) min:
0.03 = \( k[A]_0 e^{-k \times 1200} \)
Dividing equation (2) by equation (1):
\( \frac{0.03}{0.04} = e^{-k \times (1200 - 600)} \)
\( \frac{4}{3} = e^{-600k} \)
Taking natural log:
\( \ln \left( \frac{4}{3} \right) = 600k \)
Now solve for \( t_{\frac{1}{2}} \) using:
\( t_{\frac{1}{2}} = \frac{\ln 2}{k} \)
\( t_{\frac{1}{2}} = \frac{600 \ln 2}{\ln \left( \frac{4}{3} \right)} \) sec.
Now using the given values:
\( t_{\frac{1}{2}} = 600 \times \frac{\log 2}{\log 4 - \log 3} = 10 \times \frac{0.3010}{0.6020 - 0.4771} \) min
\( t_{\frac{1}{2}} = 24.08 \) min
\( t_{\frac{1}{2}} = 24 \)
The problem asks for the half-life of a first-order reaction, given the reaction rates at two different times.
For a first-order reaction, the rate of reaction is directly proportional to the concentration of the reactant at that instant. Let the reaction be \( A \rightarrow \text{Products} \).
The rate law is given by:
\[ \text{Rate} = k[A] \]
where \(k\) is the rate constant and \([A]\) is the concentration of the reactant.
The integrated rate law for a first-order reaction is:
\[ k = \frac{2.303}{t_2 - t_1} \log_{10}\left(\frac{[A_1]}{[A_2]}\right) \]
where \([A_1]\) and \([A_2]\) are the concentrations of the reactant at times \(t_1\) and \(t_2\), respectively.
Since the rate is directly proportional to the concentration (\(\text{Rate} \propto [A]\)), we can substitute the rates in place of the concentrations in the integrated rate law:
\[ k = \frac{2.303}{t_2 - t_1} \log_{10}\left(\frac{\text{Rate}_1}{\text{Rate}_2}\right) \]
The half-life (\(t_{1/2}\)) of a first-order reaction is related to the rate constant \(k\) by the formula:
\[ t_{1/2} = \frac{0.693}{k} = \frac{2.303 \log_{10}(2)}{k} \]
Step 1: List the given information.
Step 2: Calculate the rate constant (\(k\)) of the reaction.
We use the integrated rate law expressed in terms of rates. The time interval is \(t_2 - t_1 = 20 - 10 = 10\) minutes.
\[ k = \frac{2.303}{10} \log_{10}\left(\frac{0.04}{0.03}\right) \] \[ k = \frac{2.303}{10} \log_{10}\left(\frac{4}{3}\right) \]
Using the logarithm property \(\log(\frac{a}{b}) = \log(a) - \log(b)\):
\[ k = \frac{2.303}{10} (\log_{10}(4) - \log_{10}(3)) \]
Using the property \(\log(a^n) = n\log(a)\):
\[ k = \frac{2.303}{10} (2\log_{10}(2) - \log_{10}(3)) \]
Substitute the given values for \(\log(2)\) and \(\log(3)\):
\[ k = \frac{2.303}{10} (2 \times 0.3010 - 0.4771) \] \[ k = \frac{2.303}{10} (0.6020 - 0.4771) \] \[ k = \frac{2.303}{10} (0.1249) \] \[ k \approx 0.02877 \, \text{min}^{-1} \]
The unit of the rate constant is min-1 because the time interval used was in minutes.
Step 3: Calculate the half-life (\(t_{1/2}\)) of the reaction.
Using the formula for the half-life of a first-order reaction:
\[ t_{1/2} = \frac{0.693}{k} \]
Alternatively, to avoid intermediate calculations and potential rounding errors, we can use the expression involving logarithms:
\[ t_{1/2} = \frac{2.303 \log_{10}(2)}{k} = \frac{2.303 \log_{10}(2)}{\frac{2.303}{10} (\log_{10}(4/3))} \]
The \(2.303\) terms cancel out:
\[ t_{1/2} = \frac{10 \log_{10}(2)}{\log_{10}(4/3)} \]
Substitute the log values into the simplified expression:
\[ t_{1/2} = \frac{10 \times 0.3010}{2\log_{10}(2) - \log_{10}(3)} \] \[ t_{1/2} = \frac{3.010}{2 \times 0.3010 - 0.4771} \] \[ t_{1/2} = \frac{3.010}{0.6020 - 0.4771} \] \[ t_{1/2} = \frac{3.010}{0.1249} \] \[ t_{1/2} \approx 24.099 \, \text{minutes} \]
Rounding to the nearest significant figures, the half-life is approximately 24.1 minutes.
The half-life of the reaction is 24.1 minutes.
Consider the following compounds. Arrange these compounds in a n increasing order of reactivity with nitrating mixture. The correct order is : 
Two circular discs of radius \(10\) cm each are joined at their centres by a rod, as shown in the figure. The length of the rod is \(30\) cm and its mass is \(600\) g. The mass of each disc is also \(600\) g. If the applied torque between the two discs is \(43\times10^{-7}\) dyne·cm, then the angular acceleration of the system about the given axis \(AB\) is ________ rad s\(^{-2}\).

Method used for separation of mixture of products (B and C) obtained in the following reaction is: 