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Question #44055
The Question
The specific acid-catalyzed hydrolysis of ethyl acetate in a dilute aqueous solution follows the rate law: , where is the true third-order rate constant. The rate constant follows the Arrhenius equation with an activation energy parameter .
The reaction is studied at two different temperatures, and , in a variable-volume reactor maintained at a pressure sufficient to keep the mixture entirely in the liquid state. The density of the reaction mixture is at and drops to a hypothetical value of at .
If is the observed pseudo-first order rate constant (defined by ), determine the ratio .
(Assume the total mass of the mixture and the moles of the acid catalyst remain constant, and the ester is present in trace amounts.)
Options
- A.
64
- B.
80
- C.
100
- D.
125
Check Your Answer
Correct Answer
Step-by-Step Solution
Explanation
How the Examiner Thinks
Mechanism_Trap
Don't get tricked by the process! Learn the mechanical traps used in competitive exam questions.
Concepts Behind This Question
Standard State Conditions|Pseudo-First Order Kinetics|Activation Energy Trap
Why This Question Is Tricky
Common Mistakes
This problem tests the 'Hidden Variable' of temperature-dependent molarity in pseudo-first order kinetics.
Students typically assume that the pseudo-first order rate constant () scales exactly with the true rate constant () via the Arrhenius equation, leading to the trap answer of 100.
However, incorporates the concentrations of the species in excess (solvent and catalyst).
Because molarity is temperature-dependent due to thermal expansion (density changes), the concentrations of and decrease as the solution expands at higher temperatures.
Failing to account for the dependence of the pre-exponential concentration factors leads to incorrect conclusions.
Quick Facts About This Question
Question Information
| Subject | Chemistry |
| Chapter | Thermodynamics - Class 11 Part 1 |
| Concept | Standard State Conditions |
| Difficulty | 8 |
| Cognitive Load | 7 |
| Target Solve Time | 160 sec |
| Access | Free |