Question

The gas phase irreversible reaction is carried out isothermally in a PBR      A → B The...

The gas phase irreversible reaction is carried out isothermally in a PBR      A → B

The reaction is zero order. The entering temperature is 400 K, and the entering pressure is 10 atm. The flow is turbulent. For a 10 kg PBR with a pressure drop parameter α = 0.01 kg-1, the exit conversion was found to be

0.4. What catalyst weight of the PBR will you require if you need an exit conversion of 0.8, assuming that the particle diameter is decreased by a factor of 2 so that the pressure drop parameter is now increased to α = 0.02 kg-1? Assume all other operating conditions are the same as for the base case (i.e. W = 10 kg).

Homework Answers

Answer #1

Answer: Catalyst weight of the PBR will you require if you need an exit conversion of 0.8 is

W= 20 kg

Solution-

Given data:

Reaction :

Exit conversion = 0.4 (initial case)

Know the answer?
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
Similar Questions
The gas phase reaction, 2A  B  C, is carried out in a PFR. The...
The gas phase reaction, 2A  B  C, is carried out in a PFR. The feed is equal molar in A and B and the entering temperature is 650K and the entering pressure is 21 atm. If the exit conversion is X, then the exit concentration of B (in mol/dm3 ) is:
The elementary gas phase reaction A + B C is to be carried out isothermally in...
The elementary gas phase reaction A + B C is to be carried out isothermally in a continuous reactor. Reactants are entering with a stoichiometric proportions at 10 atm and 130°C molar flow rate of 20 mol/min. The exit conversion is 90%. The following data was collected from experimental work T, K kA (min-1) 360 5.38 368 8.35 376 12.73 385 16.34 395 21.23 410 28.61 425 33.81 Estimate the rate constant and the activation energy Calculate the required volume...
The gas phase reaction: 2A+B = 3C , is carried out in an isothermal packed bed...
The gas phase reaction: 2A+B = 3C , is carried out in an isothermal packed bed reactor. The rate is first order with respect to reactants A and B (second order overall) with the rate constant of 14 [liter2 /mole kg of catalyst sec.]. The feed is 50% A, 25 % B and 25 % inert at temperature of 500 K and P = 18 atm and a total flow rate of 20 mole/sec. The exit pressure is measured to...
Part I The elementary gas phase reaction (CH3)3COOC(CH3)3 --> C2H6 + 2CH3COCH3 is carried out isothermally...
Part I The elementary gas phase reaction (CH3)3COOC(CH3)3 --> C2H6 + 2CH3COCH3 is carried out isothermally in a flow reactor. The reaction rate constant at 500C is 1x10-4 min-1 and the activation energy is 85 kJ/mol. Pure di-tert-butyl peroxide enters the reactor at 10 atm and 127oC and a molar flowrate of 2.5 mol/min. Calculate the reactor volume and space time to achieve 90% conversion in; a) PF reactor b) CSTR reactor c) Propose the diameter (Dt) and length (L)...
1- The gas phase reaction 1/2N2 + 3/2H2 -->NH3 is to be carried out isothermally. The...
1- The gas phase reaction 1/2N2 + 3/2H2 -->NH3 is to be carried out isothermally. The molar feed is 50% H2, 50% N2 at a pressure of 16.4 atm and 227oC. a) Construct a complete stoichiometric table. b) Calculate the concentrations of ammonia and hydrogen when the conversion of H2 is 60%. c) Suppose by chance the reaction is elementary with ????2 = 40 ????3 ??????.?? . Write the rate of reaction solely as a function of conversion for a...
The irreversible gas-phase reaction A + B ----> C is carried out in an isothermal (400...
The irreversible gas-phase reaction A + B ----> C is carried out in an isothermal (400 C) constant-pressure (1 atm) batch reactor in the presence of inerts (I). The initial gas composition in mole fractions is given by yA0 = 0.40; yB0 = 0.40; yC0 = 0.10; yI = 0.10. The reaction is first-order both in A and in B with a rate constant, k = 3.46 x10-2 dm3mol-1 s-1 at 400 C. (a) Set up a stoichiometric table. (b)...
The dehydration butanol of alumina is carried out over a silica alumina catalyst at 680 K....
The dehydration butanol of alumina is carried out over a silica alumina catalyst at 680 K. CH3CH2CH2CH2OH ? CH3 CH = CHCH3 + H2O The rate law is ??????? = ???????? (1 + ???????????? )2 with k = 0.065 mol/gcat•h•atm and KBu = 0.42 atm-1. R = 0.082 dm3-atm/mol/K. Pure butanol enters a thin tubed packed-bed reactor at a molar flow rate 50 kmol/hr and a pressure of 10 atm (l013 kPa). (a) What PBR catalyst weight is necessary to...
The follow second order, irreversible gas phase reaction AB --> A + B, where k=2.0X10^4 cm^3/mol.min...
The follow second order, irreversible gas phase reaction AB --> A + B, where k=2.0X10^4 cm^3/mol.min is allowed to decompose isothermally in a constant pressure batch reactor. The reactor initially contains pure AB with a volume of 2.0 m^3 at 2.5 atm and 500 C. Assume ideal behavior, determine the time for the reaction to reach 70% conversion (Given R = 82.05 atm cm^3/mol.K) Answer= 4.39 min.
1. A ⇄ B + C The above gas phase elementary reversible reaction is carried out...
1. A ⇄ B + C The above gas phase elementary reversible reaction is carried out isothermally at CSTR at 640°C. The molar flow rate of raw material A is FA0 = 3.34 mol / min and the input concentration is CA0 = 0.04 mol / L. The reaction rate constant kA at 640 ° C is 0.1 mol / (Lꞏminꞏatm). When the equilibrium constant KP is 10 atm, find the corresponding equilibrium conversion Xe and calculate the reactor volume...
The irreversible gas-phase non-elementary reaction A + 2B ---> C takes place in an isothermal (227...
The irreversible gas-phase non-elementary reaction A + 2B ---> C takes place in an isothermal (227 C) constant-volume batch reactor. The initial feed to the reactor consists of 40 mol% A and 60 mol% B at a total pressure of 10 atm. Measurements of the rate of reaction as a function of conversion yielded the following results: -rA (mol dm^-3 s^-1) x (1x10^8) 0.010 0.005 0.002 0.001 XA   0.0 0.2 0.4 0.6 Calculate the time required to achieve a conversion...