Question

Exercise 4.4: Catalyst deactivation in a batch reactor Consider the irreversible, liquid-phase isomerization reaction carried
0 0
Add a comment Improve this question Transcribed image text
Answer #1

Date : GIVEN: A - >B n= 1 kalk BATCH REACTOR SOLUTION : for more balance, 1 Moles of A) - 1 Moles of A) + / Moles of A) =

Date : (RA) = d (NA/U). clt (CA) = dCA (since Ni-_ c) dit from rate law- we know that - Also (SA) = - kaca Theore, kereta Int

Date : Lê Cao = a + a. = a - Co . KA Therefore, - ln CA = ek en (ltkat) + ln Cho On rearrangement, CA = Co. (1+ kat) * © CA =

Date : @ for conversion 75% CA = (CAO) Therefore, 0.6 0.8875 a | Cao : Có ( 1+ (0-8878) + ) Bí On solving t = 9.629 ho]

Add a comment
Know the answer?
Add Answer to:
Exercise 4.4: Catalyst deactivation in a batch reactor Consider the irreversible, liquid-phase isomerization reaction carried out...
Your Answer:

Post as a guest

Your Name:

What's your source?

Earn Coins

Coins can be redeemed for fabulous gifts.

Not the answer you're looking for? Ask your own homework help question. Our experts will answer your question WITHIN MINUTES for Free.
Similar Homework Help Questions
  • The second order gas phase irreversible reaction: 2.4-B is carried out in an isothermal batch reactor...

    The second order gas phase irreversible reaction: 2.4-B is carried out in an isothermal batch reactor containing 40 kg of catalyst and with an initial volume of 60-liter. The reactor is initially filled with equal molar quantities of A and inert I at 300 K and 2.5 atm. Calculate the time needed for the concentration of product (B) to be 0.02 mole/liter if: a) the reaction takes in a constant pressure batch reactor (3 points) b) the reaction takes place...

  • QUESTION 3: 10 marks A liquid phase isomerization reaction A--> was carried out in a Packed-...

    QUESTION 3: 10 marks A liquid phase isomerization reaction A--> was carried out in a Packed- 10 points bed Reactor with a solid catalyst. The reaction is very fast and the overall rate-controlling step is the external mass transfer between catalyst surface and the bulk fluid. Recently, market demand for the product has fallen by 50%, due to Covid-19 pandemic. Therefore, the management has decided to cut the production by half so that the raw material consumption can be reduced...

  • An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second...

    An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second order in A. The feed is equimolar A and solvent (S, which contains catalyst), and enters the reactor at a total volumetric flow rate of 10 dm3/min at a concentration of A of 4 mol/L. The feed enters at 300 K. The product and reactant heat capacities are 15 cal/(mol°C), the solvent is 18 cal/(mol°C). The reaction rate constant at 300 K...

  • 2. The irreversible gas phase reaction A B is carried out isothermally in a fluidized catalytic...

    2. The irreversible gas phase reaction A B is carried out isothermally in a fluidized catalytic CSTR. The reaction rate is first orderw.r.t.the partial pressure of A (-rA KA PA). With arn entering pressure 20 atm, an negligible pressure drop in CSTR, and 50 kg of catalyst, a conversion of 50% was realized for pure A feed. |-Fluidized hal oooo -catalyst o ojo | |,'-/ pellets Now, a PBR is connected to the downstream of this CSTR with a same...

  • An aqueous phase reversible reaction ? ⇌ ? + ? is carried out in a batch...

    An aqueous phase reversible reaction ? ⇌ ? + ? is carried out in a batch reactor. The forward reaction is first order wrt A and the backward reaction is first order wrt each component. Initial concentration of A is 1 mol/litre and no R and S are present initially. Derive an expression for ?? ⁄??. What is the maximum allowable conversion in the reactor? If this reaction happens in gas phase (constant pressure), derive an expression for ?? ⁄??....

  • 3. The endothemic irreversible 2nd order reaction A +B C is carried out in a pressurised...

    3. The endothemic irreversible 2nd order reaction A +B C is carried out in a pressurised adiabatic batch reactor. The initial temperature is 120°C and the initial concentrations of both A and B are 2.0 kmol m2 Kinetic studies showed that the reaction rate constant is given by: 6000 k 2 x 105 exp(- m3kmol 1s1 T (8) (a) Derive the mass and energy balances for the reactor. Calculate the conversion achieved and the reactor temperature (b) (12) after 30...

  • The elementary irreversible organic liquid-phase reaction. a+b==>c is carried out adiabatically in a flow reactor. An...

    The elementary irreversible organic liquid-phase reaction. a+b==>c is carried out adiabatically in a flow reactor. An equal molar feed in A and 8 enters at 27'C, and the volumetric flow rate is 2 dm3/sa nd CAo= 0.I k molfm3 graphically.on exal

  • The irreversible elementary gas-phase reaction A + B ) C + D is carried out isothermally...

    The irreversible elementary gas-phase reaction A + B ) C + D is carried out isothermally at 305K in a packed bed reactor with 100 kg catalyst of particle size 8 mm. The entering pressure is 20 atm and the exit pressure is 2 atm. The feed rate is equal molar in A and B and the flow is in the turbulent flow regime, with FA0-10 mol/min and CA 0.4 mol/dm3. Currently 80% conversion is achieved. a) What would be...

  • advanced CRE subject step by step answer QUESTION 3: 10 marks A liquid phase isomerization reaction...

    advanced CRE subject step by step answer QUESTION 3: 10 marks A liquid phase isomerization reaction A--> was carried out in a Packed- 10 bed Reactor with a solid catalyst. The reaction is very fast and the overall rate-controlling step is the external mass transfer between catalyst surface and the bulk fluid. Recently, market demand for the product has fallen by 50%, due to Covid-19 pandemic. Therefore, the management has decided to cut the production by half so that the...

  • The production of methyl bromide is an irreversible liquid-phase reaction that follows an elementary rate law. The reaction CNBr (A) + CH3NH2 (B)àCH3Br (C) + NCNH2 (D) is carried out isothermally in...

    The production of methyl bromide is an irreversible liquid-phase reaction that follows an elementary rate law. The reaction CNBr (A) + CH3NH2 (B)àCH3Br (C) + NCNH2 (D) is carried out isothermally in a semi-batch reactor. A solution of methylamine (B) in extra dry ethanol at a concentration of 0.025 mol/L is to be fed at a rate of 0.05 L/s to an solution of bromine cyanide (A) in extra dry ethanol contained in a glass-lined reactor. The initial volume of...

ADVERTISEMENT
Free Homework Help App
Download From Google Play
Scan Your Homework
to Get Instant Free Answers
Need Online Homework Help?
Ask a Question
Get Answers For Free
Most questions answered within 3 hours.
ADVERTISEMENT
ADVERTISEMENT