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The gas-phase reaction with a mixture of 75% A and 25% inert is carried out isothermally...
A 200 dm3 batch reactor is pressurized to 20 atm with a mixture of 35% A,...
A 200 dm3 batch reactor is pressurized to 20 atm with a mixture of 35% A, 40% B, and 25% inert. A gas phase reaction A + BC is carried out isothermally at 227 °C. We need to compare the performance of the reactor operating at (i) Constant Volume and (ii) Constant Pressure. (a) If the reaction is first order -rAEkCA with k0.1 min-1 Calculate the time necessary to consume 99% of A. Plot NA as a function of time...
Question 10 The gas phase reaction 2A →B + C is carried out isothermally in a...
Question 10 The gas phase reaction 2A →B + C is carried out isothermally in a 30 dm3 well-mixed constant volume batch reactor. Pure A at an initial amount of 66.3 moles/dm3is placed into the reactor. If the rate of destruction of A is given by –rA = kCA, with k = 0.08 min-1, determine the concentration of A (in moles/dm3) after 5 minutes. Note that concentration is moles divided by volume. Express your answer to one decimal place.
energy il Camor P5-30 Pressure Drop. The gas phase reaction A+B C+D is carried out isothermally...
energy il Camor P5-30 Pressure Drop. The gas phase reaction A+B C+D is carried out isothermally at 227 C in a packed-bed reactor with 100 kg of catalyst. The reaction is first order in A and first order in B. The entering pres- sure was 20 atm and the exit pressure is 1 atm. The feed is equal molar in A onigA and B and the flow is in the turbulent regime with FA0 10 mol/min and CAO= 0.25 mol/dm3....
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...
The elementary gas-phase reaction A+B <----> 2C in P11-8B is now continued and carried out in...
The elementary gas-phase reaction A+B <----> 2C in P11-8B
is now continued and carried out in a packed bed reactor. The
entering molar flow rates are Fao=5 mol/s, Fbo= 2Fao, and Fi=2Fao
with Cao=0.2 mol/dm^3. The entering temperature is 325 K and a
coolant fluid is available at 300 K.
P12-9A Algorithm for reaction in a PBR with heat effects and pressure drop he elementary gas-phase reaction A+B 2C in P11-8B is now continued and carried out in packed-bed reactor....
a catalytic reaction of gas phase A-R is carried out in a PFR containing 0.01 kg...
a catalytic reaction of gas phase A-R is carried out
in a PFR containing 0.01 kg of solid catalyst, feed rate, Fao =
1500mol / hour. the reactor is operated at 3.2 atm and 117 C.
kinetics data are shown in the following table
determine :
a. reaction order
b.weight of catalyst required of conversion is 35%
uToper 3 2 Run 0,040 0,038 0,060 0,080 0,100 0,084 CAins mol/liter 0,055 0,070 Caut mol/liter
Problem 2 (30 points) For the gas phase reaction below, calculate the conversion in the CSTR,...
Problem 2 (30 points) For the gas phase reaction below, calculate the conversion in the CSTR, if weight of catalyst in PFR (Wi) is equal to the weight of the catalyst in CSTR (W2) Note the difference in reaction conditions AB+C FAO = 10mol's CAO 0.1 mol/dm3 T-325 K;E 2500 cal FAO =10mol s CAO 0.1 ol/dm3 T = 350 K What is the conversion of the CSTR?
Question 4. A gas phase reaction of the type A+B - C, is to be carried...
Question 4. A gas phase reaction of the type A+B - C, is to be carried out isothermally in a PFR. A feed consisting of 90% of A and 10% of B enters the reactor at a temperature of 27 °C and 10 atm. The reaction is second order with respect to A and zero order with respect to B. The rate constant, ka, is 1.5 dm²/mol.s. a) Calculate the volume required to achieve 60% conversion of A for an...
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...
a catalytic reaction of gas phase A-R is carried out in a PFR containing 0.01 kg...
a catalytic reaction of gas phase A-R is carried out
in a PFR containing 0.01 kg of solid catalyst, feed rate, Fao =
1500mol / hour. the reactor is operated at 3.2 atm and 117 C.
kinetics data are shown in the following table
determine :
a. reaction order
b.weight of catalyst required of conversion is 35%
uToper 3 2 Run 0,040 0,038 0,060 0,080 0,100 0,084 CAins mol/liter 0,055 0,070 Caut mol/liter
uToper 3 2 Run 0,040 0,038 0,060...
A 200 dm3 batch reactor is pressurized to 20 atm with a mixture of 35% A, 40% B, and 25% inert. A gas phase reaction A + BC is carried out isothermally at 227 °C. We need to compare the performance of the reactor operating at (i) Constant Volume and (ii) Constant Pressure. (a) If the reaction is first order -rAEkCA with k0.1 min-1 Calculate the time necessary to consume 99% of A. Plot NA as a function of time...
energy il Camor P5-30 Pressure Drop. The gas phase reaction A+B C+D is carried out isothermally at 227 C in a packed-bed reactor with 100 kg of catalyst. The reaction is first order in A and first order in B. The entering pres- sure was 20 atm and the exit pressure is 1 atm. The feed is equal molar in A onigA and B and the flow is in the turbulent regime with FA0 10 mol/min and CAO= 0.25 mol/dm3....
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...
The elementary gas-phase reaction A+B <----> 2C in P11-8B
is now continued and carried out in a packed bed reactor. The
entering molar flow rates are Fao=5 mol/s, Fbo= 2Fao, and Fi=2Fao
with Cao=0.2 mol/dm^3. The entering temperature is 325 K and a
coolant fluid is available at 300 K.
P12-9A Algorithm for reaction in a PBR with heat effects and pressure drop he elementary gas-phase reaction A+B 2C in P11-8B is now continued and carried out in packed-bed reactor....
a catalytic reaction of gas phase A-R is carried out
in a PFR containing 0.01 kg of solid catalyst, feed rate, Fao =
1500mol / hour. the reactor is operated at 3.2 atm and 117 C.
kinetics data are shown in the following table
determine :
a. reaction order
b.weight of catalyst required of conversion is 35%
uToper 3 2 Run 0,040 0,038 0,060 0,080 0,100 0,084 CAins mol/liter 0,055 0,070 Caut mol/liter
Problem 2 (30 points) For the gas phase reaction below, calculate the conversion in the CSTR, if weight of catalyst in PFR (Wi) is equal to the weight of the catalyst in CSTR (W2) Note the difference in reaction conditions AB+C FAO = 10mol's CAO 0.1 mol/dm3 T-325 K;E 2500 cal FAO =10mol s CAO 0.1 ol/dm3 T = 350 K What is the conversion of the CSTR?
Question 4. A gas phase reaction of the type A+B - C, is to be carried out isothermally in a PFR. A feed consisting of 90% of A and 10% of B enters the reactor at a temperature of 27 °C and 10 atm. The reaction is second order with respect to A and zero order with respect to B. The rate constant, ka, is 1.5 dm²/mol.s. a) Calculate the volume required to achieve 60% conversion of A for an...
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...
a catalytic reaction of gas phase A-R is carried out
in a PFR containing 0.01 kg of solid catalyst, feed rate, Fao =
1500mol / hour. the reactor is operated at 3.2 atm and 117 C.
kinetics data are shown in the following table
determine :
a. reaction order
b.weight of catalyst required of conversion is 35%
uToper 3 2 Run 0,040 0,038 0,060 0,080 0,100 0,084 CAins mol/liter 0,055 0,070 Caut mol/liter
uToper 3 2 Run 0,040 0,038 0,060...
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