The decomposition of NH3 on platinum surface is zero order reaction. If k = 2.5 × 10-4 mol L-1 s-1 the rate of production of H2 is
The question describes the decomposition of ammonia (\(\text{NH}_3\)) on a platinum surface as a zero-order reaction. This means the rate of the reaction is independent of the concentration of the reactant (\(\text{NH}_3\)). The rate constant (\(k\)) for this reaction is given as \(2.5 \times 10^{-4} \, \text{mol L}^{-1} \text{ s}^{-1}\). We need to determine the rate of production of hydrogen (\(\text{H}_2\)).
The decomposition of ammonia on a platinum catalyst is represented by the following balanced chemical equation:
\[ 2\text{NH}_3\text{(g)} \xrightarrow{\text{Pt catalyst}} \text{N}_2\text{(g)} + 3\text{H}_2\text{(g)} \]For a general reaction \(aA \rightarrow bB + cC\), the rate of the reaction is defined as:
\[ \text{Rate} = -\frac{1}{a}\frac{d[A]}{dt} = \frac{1}{b}\frac{d[B]}{dt} = \frac{1}{c}\frac{d[C]}{dt} \]where \(-\frac{d[A]}{dt}\) is the rate of disappearance of reactant A, and \(\frac{d[B]}{dt}\) and \(\frac{d[C]}{dt}\) are the rates of appearance of products B and C, respectively. The coefficients \(a\), \(b\), and \(c\) are the stoichiometric coefficients from the balanced equation.
Applying this to the decomposition of ammonia:
\[ \text{Rate} = -\frac{1}{2}\frac{d[\text{NH}_3]}{dt} = +\frac{1}{1}\frac{d[\text{N}_2]}{dt} = +\frac{1}{3}\frac{d[\text{H}_2]}{dt} \]The problem states that the reaction is zero order with respect to ammonia on the platinum surface. For a zero-order reaction, the rate of the reaction is equal to the rate constant \(k\), and it does not depend on the concentration of the reactant.
\[ \text{Rate} = k \]Given \(k = 2.5 \times 10^{-4} \, \text{mol L}^{-1} \text{ s}^{-1}\).
We want to find the rate of production of \(\text{H}_2\), which is \(\frac{d[\text{H}_2]}{dt}\). From the rate expression, we have the relationship:
\[ \text{Rate} = +\frac{1}{3}\frac{d[\text{H}_2]}{dt} \]Since the Rate is equal to \(k\) for a zero-order reaction:
\[ k = \frac{1}{3}\frac{d[\text{H}_2]}{dt} \]To find the rate of production of \(\text{H}_2\), we rearrange the equation:
\[ \frac{d[\text{H}_2]}{dt} = 3 \times k \]Substitute the given value of \(k\) into the equation:
\[ \frac{d[\text{H}_2]}{dt} = 3 \times (2.5 \times 10^{-4} \, \text{mol L}^{-1} \text{ s}^{-1}) \] \[ \frac{d[\text{H}_2]}{dt} = 7.5 \times 10^{-4} \, \text{mol L}^{-1} \text{ s}^{-1} \]Thus, the rate of production of \(\text{H}_2\) is \(7.5 \times 10^{-4} \, \text{mol L}^{-1} \text{ s}^{-1}\).
Let's look at the given options:
Our calculated rate of production of \(\text{H}_2\) matches Option 2.
This problem involves several key concepts from chemical kinetics:
| Term | Definition | Relevance to Problem |
|---|---|---|
| Zero Order Reaction | Reaction rate is independent of reactant concentration. | Given property of NH3 decomposition on Pt. |
| Rate Constant (k) | Proportionality constant in the rate law. | Given value used to calculate product rate. |
| Rate of Production | Rate at which a product's concentration increases over time. | The quantity we needed to calculate for H2. |
| Stoichiometry | Coefficients in balanced equation. | Used to relate overall reaction rate to the rate of H2 formation (factor of 3). |
| Order | Rate Law Example | Rate Unit | k Unit | Integrated Rate Law Example |
|---|---|---|---|---|
| Zero Order | Rate = k | mol L-1 s-1 | mol L-1 s-1 | [A]t = [A]0 - kt |
| First Order | Rate = k[A] | mol L-1 s-1 | s-1 | ln[A]t = ln[A]0 - kt |
| Second Order | Rate = k[A]2 or Rate = k[A][B] | mol L-1 s-1 | L mol-1 s-1 | 1/[A]t = 1/[A]0 + kt |
The decomposition of ammonia on a platinum surface is an example of a heterogeneous catalytic reaction. In such reactions, the reactants are adsorbed onto the surface of the catalyst (platinum in this case). The reaction then occurs on the surface. Zero-order kinetics are often observed in heterogeneous catalysis when the reactant is strongly adsorbed onto the catalyst surface.
When the reactant is strongly adsorbed, the surface sites become saturated with reactant molecules. This means that almost all available surface sites are occupied by \(\text{NH}_3\) molecules. As more \(\text{NH}_3\) molecules approach the surface, they cannot find empty sites to adsorb onto. Therefore, increasing the concentration of \(\text{NH}_3\) in the gas phase does not lead to a significant increase in the number of adsorbed \(\text{NH}_3\) molecules on the surface, where the reaction actually happens.
Since the rate of the surface reaction depends on the amount of adsorbed reactant, and this amount is essentially constant (at saturation) regardless of the gas phase concentration, the overall reaction rate becomes independent of the gas phase \(\text{NH}_3\) concentration. This results in zero-order kinetics.
The rate constant \(k\) for such a process includes factors like the intrinsic rate constant of the surface reaction and the surface area of the catalyst.
The molecularity of the following elementary reaction is NH4NO2 → N2 + 2H2O