Question

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) Determine the time it will take for yC to reach 0.20.

Homework Answers

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
A liquid phase reaction A+B --> C+D is to be carried out in an isothermal and...
A liquid phase reaction A+B --> C+D is to be carried out in an isothermal and well mixed batch reactor. The initial moles of A and B are both 0.1 mole.  The rate of destruction of A is given by –rA = k*CA*CB, with k =  6.0 L/ (mol*min).  Calculate the amount of time (in minutes) that the reaction must proceed within a 10 L reactor in order to achieve a final concentration of A of 0.001 mol/L. Please express your answer to...
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...
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...
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...
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 elementary irreversible organic liquid-phase reaction, A + B → C, is carried out in a...
The elementary irreversible organic liquid-phase reaction, A + B → C, is carried out in a flow reactor. An equal molar feed in A and B enters at 27 oC, and the volumetric flow rate is 2 L/s. The feed concentration is CA0 = 0.1 mol/L. a) Calculate the PFR and CSTR volumes necessary to achieve 85% conversion when the reaction is carried out adiabatically. b) What is the maximum inlet temperature one could have so that the boiling point...
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 isothermal and isobaric gas phase reaction A → B + C follows an elementary rate...
The isothermal and isobaric gas phase reaction A → B + C follows an elementary rate law and is to be carried out in a CSTR. The reaction constant k = 1.20 s-1 when the reaction temperature T = 300 K. (a) When pure A is fed to a CSTR at 300K and a volumetric flow rate of 5 dm3 /s,a conversion of X = 0.6 is achieved. Please determine the volume of the CSTR. (b) If the CSTR’s volume...
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.
An isothermal CSTR with a first order irreversible reaction A —> B and rA = 0.14...
An isothermal CSTR with a first order irreversible reaction A —> B and rA = 0.14 mol/(ft3*min) has a constant flow rate of 11 f3/min. The reactor volume is 100 ft3. The inlet concentration CAi changes from 6 to 5.5 moles/ft3 (a step change). (a) Determine the process time constant. (b) Determine the steady state gain.
ADVERTISEMENT
Need Online Homework Help?

Get Answers For Free
Most questions answered within 1 hours.

Ask a Question
ADVERTISEMENT