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Question

The correct statement(s) for a surface catalyzed unimolecular gaseous reaction is(are)

Surface-Catalyzed Unimolecular Reaction Kinetics

A surface-catalyzed unimolecular gaseous reaction involves a single reactant molecule adsorbing onto a catalyst surface and then reacting to form products. The reaction rate is influenced by factors such as reactant pressure and the degree of surface coverage.

Analysis of Correct Statements

  • Statement B: Zero order kinetics at high pressure
    When the pressure of the reacting gas is sufficiently high, the catalyst surface becomes saturated with adsorbed reactant molecules. In this saturation regime, the surface concentration of adsorbed species is maximal and essentially constant. The rate-limiting step, whether it's the reaction of adsorbed molecules or their desorption, no longer depends on the external gas pressure. Consequently, the reaction exhibits zero-order kinetics with respect to the reactant pressure.
    Rate $\approx k$ (constant) at high P
  • Statement C: First order kinetics at low pressure
    Conversely, at very low pressures, the catalyst surface is sparsely populated with adsorbed reactant molecules (low surface coverage, $\theta$). The rate of reaction often depends on the number of adsorbed molecules and the availability of vacant surface sites. Under these dilute conditions, the rate is typically found to be directly proportional to the gas pressure ($P$), leading to first-order kinetics.
    Rate $\propto P$ at low P
  • Statement D: Rate proportional to surface coverage
    The rate of a surface reaction is fundamentally linked to the amount of reactant adsorbed on the catalyst surface. If the reaction mechanism involves adsorbed species, the rate ($r$) is often directly proportional to the fraction of the surface covered by the reactant molecules ($\theta$).
    r $\propto \theta$ This relationship holds under varying conditions, reflecting the dependence on available adsorbed reactant.

Explanation for Statement A

  • Statement A: Freundlich adsorption isotherm
    The behavior described by statements B and C (pressure-dependent reaction orders) is typically derived using the Langmuir adsorption isotherm model, which assumes monolayer adsorption on a homogeneous surface. While Freundlich adsorption isotherm applies to non-ideal adsorption scenarios, the Langmuir model provides the standard framework for explaining the kinetics of simple surface-catalyzed unimolecular reactions. Therefore, stating it follows Freundlich isotherm is generally not the primary or most accurate description in this context.
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Important Questions from Adsorption

  1. A volatile organic compound (VOC) is to be adsorbed from air onto a bed of activated carbon. The equilibrium capacity of activated carbon at the feed conditions is $0.4 \text{ grams}$ VOC per gram of activated carbon. The column contains $4 \text{ grams}$ of activated carbon per $\text{cm}^2$ of cross-section. The feed rate into the adsorber column is $0.2 \text{ grams}$ VOC $\text{cm}^{-2}\text{ h}^{-1}$. Breakthrough time is defined as the time at which the concentration at the exit of the bed ($c$) reaches a value of $0.05c_0$, where $c_0$ is the concentration of VOC in the feed. The breakthrough time for the bed is $2.1 \text{ h}$. The area under $c / c_0$ curve between the initial and breakthrough times is $0.1 \text{ h}$. Which one of the following is the fraction of unused bed at breakthrough?
  2. 500 mg of a dry adsorbent is added to a beaker containing 100 mL solution of concentration 100 mg phenol/(L solution). The adsorbent is separated out after 5 h of rigorous mixing. If the residual concentration in the solution after separating the adsorbent is 30 mg phenol/(L solution), the amount of phenol adsorbed (in mg per gram of dry adsorbent) is
  3. Adsorption on activated carbon is to be used for reducing phenol concentration in wastewater from 0.04 mol/l to 0.008 mol/l. The adsorption isotherm at the operating temperature can be expressed as $q = 0.025C^{1/3}$; where $q$ is the phenol concentration in solid (mol/g solid) and $C$ is the phenol concentration in water (mol/l). The minimum amount of solid (in grams) required per liter of wastewater (up to one decimal place) is ________
  4. At 30°C, the amounts of acetone adsorbed at partial pressures of 10 and 100 mmHg are 0.1 and 0.4 kg acetone/kg activated carbon, respectively. Assume Langmuir isotherm describes the adsorption of acetone on activated carbon. What is the amount of acetone adsorbed (in kg per kg of activated carbon) at a partial pressure of 50 mmHg and 30°C?
  5. At 273 K and 10 bar, the Langmuir adsorption of a gas on a solid surface gave the fraction of surface coverage as 0.01. The Langmuir adsorption isotherm constant is ________ bar$^{-1}$. (Give the answer to the third decimal place)

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