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Question #44850

Difficulty: 8/10 | 🟢 Free

The Question

A rigid reactor of volume 8.0 L8.0 \text{ L} contains a solid tungsten catalyst with a total active surface area of 40.0 cm240.0 \text{ cm}^2. The decomposition of \ce{NH3(g)} on the catalyst surface at 1000 K1000 \text{ K} and an initial pressure of 50 atm50 \text{ atm} follows zero-order kinetics due to complete surface saturation (Langmuir-Hinshelwood mechanism).

The catalyst surface has a site density of 1.5×1019 active sites m−21.5 \times 10^{19} \text{ active sites m}^{-2}. The rate-determining step is the decomposition of adsorbed \ce{NH3}, which occurs with a transition state vibrational frequency of ν=4.0×1012 s−1\nu = 4.0 \times 10^{12} \text{ s}^{-1}.

Given the activation energy for the surface reaction is Ea=23.03RTE_a = 23.03 RT, calculate the magnitude of the initial rate of change of the partial pressure of \ce{NH3(g)} in the reactor.

(Assume ideal gas behavior, NA=6.0×1023 mol−1N_A = 6.0 \times 10^{23} \text{ mol}^{-1}, R=0.08 L atm K−1 mol−1R = 0.08 \text{ L atm K}^{-1} \text{ mol}^{-1}, and e−23.03=10−10e^{-23.03} = 10^{-10}. Each active site decomposes one \ce{NH3} molecule per effective vibration.)

Options

  • A.

    4.0×10−4 atm s−14.0 \times 10^{-4} \text{ atm s}^{-1}

  • B.

    8.0×10−1 atm s−18.0 \times 10^{-1} \text{ atm s}^{-1}

  • C.

    4.0 atm s−14.0 \text{ atm s}^{-1}

  • D.

    4.0×10−5 atm s−14.0 \times 10^{-5} \text{ atm s}^{-1}

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Explanation

How the Examiner Thinks

Numerical_Precision

Improve calculation stamina and avoid rounding errors in high-stakes competitive examinations.

Concepts Behind This Question

Units of Rate Constant (k)|Collision Frequency vs. Effective Collisions|Zero Order Rate Integration

Why This Question Is Tricky

Common Mistakes

The problem tests the 'Hidden Variable' of dimensionality in heterogeneous catalysis.

Students often memorize the Arrhenius equation and zero-order kinetics in terms of volumetric concentration (mol L−1 s−1\text{mol L}^{-1} \text{ s}^{-1}).

Here, the 'effective collision' frequency is limited by the 2D surface site saturation, meaning the pre-exponential factor AA and rate constant kk must be defined per unit area (mol m−2 s−1\text{mol m}^{-2} \text{ s}^{-1}).

Failing to account for the catalyst's surface area or incorrectly treating AA as a volumetric parameter leads to massive dimensional and numerical errors (as seen in the distractors).

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Question Information

SubjectChemistry
ChapterChemical Kinetics - Class 12
ConceptUnits of Rate Constant (k)
Difficulty8
Cognitive Load7
Target Solve Time160 sec
AccessFree