Question

Question 2: a- Consider the elementary liquid-phase reaction: A ? B Taking place in A PFR....

Question 2:

a- Consider the elementary liquid-phase reaction: A ? B Taking place in A PFR. Determine the space-time taken to reach 80% conversion of A. The value of k is 2.3 s -1 .

b- The first-order reaction A? B is carried out in a batch reactor with k = 0.3 min-1 , what is the time (in min) required to consume 90% of A?

c- Plot the conversion X against time for the reaction described in b by assuming a first order reaction then a second order reaction.

Question 3: Describe in your own words a quantum chemistry procedure that can be applied to calculate reaction enthalpies.

Homework Answers

Answer #1

a) mean residence time ( or space time) defined by ? = V/ v0

For first order PFR this can be written as

? = ? 1 /k * ln (1 ? X) .Solving this spact time = -1/2.3* ln(1-.8) =0.69975 min

b)Rate constant for first order ,rate constant(k) = ln{[A0]/[A]}/t

So time tequired t = ln{[A0]/[A]} /k = ln{100/(100-90) }/0.3 =7.675 min

C)To plot first order ratio use t = ln{[A0]/[A]} /k = put conversion 5 to 95 % and calculate time for all

For 5% conversion t= 0.17097 minute

15 %  conversion t= 0.5417 minute

30 %  conversion t= 1.1889 minute

45%  conversion t= 1.99279 minute

60%  conversion t= 3.054 minute

75%  conversion t= 4.62098minute

90%  conversion t= 7.675 minute

95%  conversion t= 9.9857minute

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
he elementary liquid-phase reaction: A + B -----> C is to be carried out non-isothermally in...
he elementary liquid-phase reaction: A + B -----> C is to be carried out non-isothermally in a flow system with reaction constant,k= 0.07 dm^3mol-1min-1at 300K. The concentrations of each feed stream of A and B is 2 mol dm-3. The volumetric flow rate of each feed stream is 5 dm^3min-1. The two steams are mixed immediately prior to entering the reactor system. This flow system is conducted at 300K with two reactors: a 200 dm^3 stainless steel CSTR and an...
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...
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 liquid phase reaction takes place in an adiabatic flow reactor. ? + ? →...
The elementary liquid phase reaction takes place in an adiabatic flow reactor. ? + ? → ? An equimolar feed in A and B enters at 300K, and the volumetric flow rate is 2 dm3 /s and CA0= 100 mol/m3 . a) Calculate the PFR and CSTR volumes to achieve 75 % conversion. b) If the outlet temperature of the reactor is 550 K, for complete conversion, calculate the inlet temperature of CSTR. HA°(273 K) = - 20 kcal/mol, HB°...
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...
Problem 1 Consider the liquid phase reaction A à products accelerated by a homogeneous catalyst dissolved...
Problem 1 Consider the liquid phase reaction A à products accelerated by a homogeneous catalyst dissolved in the solution. The observed rate data follows the form: -r=k1Ca/(1+K2Ca+K3(Ca^2)) You are asked to recommend either a steady CSTR or steady PFR. Your reactor must reduce the feed composition of 0.6 mole/liter down to 0.3 mole/liter in the effluent. • Create a plot of ordinate 1/(-rA) vs. abscissa CA. Use the data below. Use sufficient resolution in your plot to get a smooth...
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  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:
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)...
A homogeneous liquid phase reaction A -> R, rA = -kCA^2 takes place with 50% conversion...
A homogeneous liquid phase reaction A -> R, rA = -kCA^2 takes place with 50% conversion in a mixed reactor (CSTR). What will be the conversion if this reactor is replaced by one 6 times as large-all else remaining unchanged?
ADVERTISEMENT
Need Online Homework Help?

Get Answers For Free
Most questions answered within 1 hours.

Ask a Question
ADVERTISEMENT