CHEMMAT 303 Auckland Chemical Engineering Heterogeneous Catalytic Reactors Discussion

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Yvmmn10385910

Engineering

CHEMMAT 303

The University of Auckland

CHEMMAT

Description

This is a 2 hour constrained assignment but I have been able to get the questions first due to aegrotat. Ddl would be in around 40 hours, so 8pm EST 25th/10 for time conversion.

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Question 1 [40 marks] In presence of spherical catalyst pellets, an experimental decomposition rate of gaseous A in a packed bed reactor follows the kinetics: - r’’’A, obs = 1.1 x105 mol/m3cat.hr (a) Derive an equation to evaluate the effects of non-isothermal behavior across the stagnant gas film surrounding spherical pellets (external heat transfer). (10 marks) (b) With the given data, shown below, determine the temperature variations across the stagnant gas film. • Diameter of the pellets, dp = 7 mm • Effective diffusivity, De = 5 x10-5 m3/mcat.hr • Heat transfer coefficient, h = 150 kJ/m2cat.K.hr (for the gas film). • Heat of reaction, ∆Hr = -120 kJ/mol A (exothermic). (10 marks) (c) Which parameters should be optimized to reduce the temperature variations? (5 marks) (d) If the decomposition takes place based on the catalyst volume with the reaction constant: 𝑘𝑘 ′′′ = 5 m3fluid. m-3cat. s-1 Calculate the reaction constant,𝑘𝑘 ′′′′ , based on the reactor volume, given that: • The bulk density of the packed bed is 2100 kg/m3, and • The void is 0.56 m3voids/m3 reactor (15 marks) Page 2/3 Question 2 [60 marks] In a CSTR of 0.25 m3 volume, liquid is being fed at 0.5 m3/hr with 12 mol/m3 concentration of the reactant A according to the catalytic reaction shown below. −𝑟𝑟𝐴𝐴′ = 0.003 𝐶𝐶𝐴𝐴 𝑚𝑚𝑚𝑚𝑚𝑚. 𝑘𝑘𝑘𝑘−1 . ℎ𝑟𝑟 −1 The catalyst bulk density is 1760 kg.m-3 and the particle density is 2000 kg.m-3. Assume external and internal mass transfer resistances are negligible. (a) What is the conversion of the reactant in the CSTR when the catalyst is fresh? (20 marks) (b) Based on a pilot-plant experiment, the catalyst being used has a third order deactivation kinetics: 𝑑𝑑𝑑𝑑 − 𝑑𝑑𝑑𝑑 = 𝑘𝑘𝑑𝑑 𝑎𝑎3 (unit of Kd is day-1) It is found out that the catalyst is deactivating sharply, and that after 7 days, the conversion, XA, has dropped to 60%. What is the deactivation rate constant, kd? (20 marks) (c) Assume you want to regenerate the catalyst when the conversion, XA, drops equal to or below 70%. For how many days should you operate the reactor before regenerating the catalyst? Is it technically feasible? (20 marks) Page 3/3
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Explanation & Answer

Hey buddy! I just saw that you will be passing this hours from now so I prioritized this to be answered. Pls review this and I hope I gave every detail in my solution. Thank you so much buddy for choosing me as your tutor. If you have any questions regarding chemical engineering pls invite me to answer you questions. I hope to work with you again in the future buddy. Always take care and Bye!

Running Head: CHEMICAL REACTOR

Chemical Reactor
Name:
Course:
Instructor:
Date:

2
CHEMICAL REACTOR
Question 1

Solution
a) For change in temperature in the surrounding film (ΔTf) we equate the rate of heat removal
through the film with the rate of heat generation by reaction within the pellet.
𝑸𝒈𝒆𝒏𝒆𝒓𝒂𝒕𝒆𝒅 = 𝑸𝒓𝒆𝒎𝒐𝒗𝒆𝒅
𝑸𝒈𝒆𝒏𝒆𝒓𝒂𝒕𝒆𝒅 = 𝑽𝒑𝒆𝒍𝒍𝒆𝒕 ∗ (−𝒓𝑨 ′′′ ,𝒐𝒃𝒔 )(∆𝑯𝒓 )
𝑸𝒓𝒆𝒎𝒐𝒗𝒆𝒅 = 𝒉𝑺𝒑𝒆𝒍𝒍𝒆𝒕 ∗ (𝑻𝒈 − 𝑻𝒔 )
𝑽𝒑𝒆𝒍𝒍𝒆𝒕 ∗ (−𝒓𝑨 ′′′ ,𝒐𝒃𝒔 )(∆𝑯𝒓 ) = 𝒉𝑺𝒑𝒆𝒍𝒍𝒆𝒕 ∗ (𝑻𝒈 − 𝑻𝒔 )
(𝑻𝒈 − 𝑻𝒔 ) =

𝑽𝒑𝒆𝒍𝒍𝒆𝒕 ∗ (−𝒓𝑨 ′′′ ,𝒐𝒃𝒔 )(∆𝑯𝒓 )
𝒉𝑺𝒑𝒆𝒍𝒍𝒆𝒕

𝟒 𝟑
𝝅𝒓 ,
𝑺𝒑𝒆𝒍𝒍𝒆�...


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