Constant Volume and Constant Pressure Batch Reactor

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SUMMARY

The discussion focuses on the analysis of two types of batch reactors for the decomposition of A to B: a constant volume reactor (reactor 1) and a constant pressure reactor (reactor 2). For reactor 1, the fractional decrease in concentration of A after 5 minutes is calculated using the first-order reaction equation, resulting in the expression C_A/C_{A0} = exp(-kt). In contrast, reactor 2 requires the application of the Laplace transform of the Ideal Gas equation to derive the concentration over time, leading to an error function representation. The key equations and transformations necessary for solving both parts of the problem are emphasized.

PREREQUISITES
  • Understanding of first-order reaction kinetics
  • Familiarity with Laplace transforms
  • Knowledge of the Ideal Gas Law
  • Basic calculus for integration and differential equations
NEXT STEPS
  • Study the application of Laplace transforms in chemical kinetics
  • Learn about the Ideal Gas Law and its assumptions
  • Explore error functions and their applications in concentration calculations
  • Investigate the differences between constant volume and constant pressure systems in chemical reactions
USEFUL FOR

Chemical engineers, students studying reaction kinetics, and professionals involved in reactor design and analysis will benefit from this discussion.

missmaria
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Homework Statement


Consider the following two well-mixed, isothermal batch reactors for the elementary and irreversible decomposition of A to B, A\stackrel{k}{\rightarrow}2B
reactor1: The reactor volume is constant (Pressure is variable)
reactor2: The reactor pressure is constant (Volume is variable)
Both reactors are charged with pure A at 1.0 atm and k=0.35min^{-1}

a) what is the fractional decrease in the concentration of A in reactors 1 and 2 after 5 minutes?
b)what is the total molar conversion of A in reactors 1 and 2 after 5 minutes?



Homework Equations



Since reaction is first order: r_{A}=-kC_{A}

The Attempt at a Solution



Ok, so part a for a constant volume reactor was simple, since the ODE was easy and it turned out that \frac{C_{A}}{C_{A0}}=exp(-kt)
but variable volume has me stumped. I figured out that -k=\frac{dC_{A}}{dt}+(\frac{1}{V})(\frac{dV}{dt} but i don't know where to go from here.

I don't even know where to start for part b, please help...
 
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This problem is a bit complicated, but I remember it from my days as an undergraduate. You have to use a Laplacian transform of the Ideal Gas equation (assuming that T is high enough at 1atm to support this assumption). This should give you an equation for concentration in the form of a Gaussian, which, when integrated, will give an error function. You should work this out for yourself, but your answer should be of the form:

Ca / Cao = erf(-Vr * k * t)

Hope this helps.
 
I'm not sure i understand what exactly you mean, could you spell it out stepwise?
 
just kidding. You actually use the Ideal gas equation and (think about the assumptions made for the ideal gas law) calculate delta(V). Then, think about what Cj means
 

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