Tutorial 4 - 2013

From Introduction to Reactor Design: 3K4
Jump to: navigation, search
Due date(s): All questions due as assignment 3A
Nuvola mimetypes pdf.png (PDF) Tutorial questions

Assignment objectives

Assignment objectives:

  • To demonstrate your understanding of chemical equilibrium in system with and without change in volume.
  • To use the reactor design equations in terms of conversion.

Question 1 [5]

Consider the reversible reaction of A going to 2B, with only pure A fed to the flow reactor at 340K and 202.6 kPa. The equilibrium constant at 340K is \(K_C = 100\,\text{mol.m}^{-3}\).

Show that the equilibrium conversion, \(X_\text{eq}\), leaving the reactor is \(X_\text{eq} = 0.51\).

Question 2 [4]

Consider the system producing product, D, from raw materials A and B in the reversible reaction:

\[\text{A} + \text{B} \mathop{\rightleftharpoons}_{k_{-A}}^{k_A} \text{D}\]

If the equilibrium constant, \(K_C\) has a value of 40 at room temperature, 25°C:

  1. What are the units of \(K_C\)?
  2. What is the value of \(K_C\) at 50°C, if the heat of reaction is \(150\,\text{kJ.mol}^{-1}\)?
  3. Draw of a plot of the equilibrium constant against temperature.

Question 3 [20]

At your company there is an existing glass-lined, and well-mixed CSTR. With the inlet and outlet valves closed it becomes a batch reactor. The volume of this vessel is 1800 L. The temperature of the vessel is easily controlled.

You are working to produce a product, D, from raw materials A and B in the reaction:

\[\text{A} + \text{B} \mathop{\longrightarrow}^{k_A} \text{D}\]

which is a liquid-phase reaction system that operates with the following kinetics: \(-r_A = k_A C_A\), where \(k_A = 0.18\,\text{hour}^{-1}\) helpfully determined by your company's laboratory, at room temperatures of 25°C.

Your boss is giving you, the engineering team lead, the task of determining how to maximize production of species D. Because there is such a high demand for it, you must figure out how to produce the most amount of D within a regular production shift in that vessel. Species A is available in pure form at 50 mol per litre, and species B is available at 70 mol per litre.

There is only one constraint: you must operate at room temperature, because the product is extremely temperature sensitive and starts to degrade rapidly at temperatures exceeding 30°C. Also consider that you want the stream leaving the reactor to have a high purity, so you can minimize the amount of downstream separation of D from A and B.

Describe clearly and concisely to your operators how to produce product D and how much of D will be produced in a 12 hour period. You must show all your calculation steps to obtain full grade.

Question 4 [12]

The following gas phase reaction is taking place: \(\text{A} \longrightarrow 3\text{B}\) at 350K and 900 kPa; the equilibrium constant is \(0.20\,\text{mol}^2\text{.L}^{-6}\) at these conditions. Calculate (a) the equilibrium concentration of A, (b) the equilibrium concentration of B, and (c) the conversion of A, for the following 3 cases:

  1. The material is reacting in a flow reactor.
  2. The material is reacting in a constant volume batch reactor.
  3. The material is reacting in a constant pressure batch reactor.


  1. Compare the above answers for the 3 situations and explain why they make sense/do not make sense. In particular, explain any differences in the equilibrium concentration of A among the 3 reactors.