Consider gas phase reaction carried out in variable volume PFR
$$ 4 \mathrm{~A}+2 \mathrm{~B} \rightarrow 2 \mathrm{C} $$
The entering pressure and temperature are \(15 \mathrm{~atm}\) and \(227^{\circ} \mathrm{C}\) respectively. If the feed is equal molar in \(\mathrm{A}\) and \(\mathrm{B}\), determine the concentration of \(\mathrm{B}\) at the exit. Assume no pressure drop during the reaction.
Hi everybody,can you help me for problem 4 in the attach . Thank
for help!
The elementary reversible reaction A + B 2C occurs in the liquid phase in isothermal CSTR. A stream containing equimolar amounts of A and B in a solvent enters. the reactor, and the conversion of A is measured to be 60%. The equilibrium conversion o A under the same inlet conditions is known to be 80%. The volumetric flowrate into the process is to be...
(3) The gas phase reaction 2A +B- C is carried out in an isothermal PFR without pressure drop. At the entrance, the feed contains 1/2 molar fraction of A, 1/3 molar fraction of B and 1/6 molar fraction of inert chemical I. The entrance temperature is 500K and the entrance pressure is 16.4 atm. If the conversion of A at the exit is 0.8, what is the conversion of B?
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....
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...
Kinetic reactions
Please make sure you get the same answers as written and
solve all the parts
Thanks in advance
3. The elementary gas-phase reaction A → B + 2C gives a rate constant of 10-4 min-1 at 50°C and has an activation energy of 85 kJ mol1. This reaction is carried out in a flow reactor that is operated isothermally at 127 °C with a negligible pressure drop. The reactor feed is pure A, entering at 127 °C and...
Question 1: Design of isothermal reactors 30 Marks The irreversible, gas-phase reaction A+B D is to be carried out in an isotherma °C) plug-flow reactor (PFR) at 5.0 atm. The mole fractions of the feed streams are A 0 B 0.50, and inerts 0.30. The activation energy for the above reaction is 80 000 cal/mol. the pressure drop due to fluid friction in the reactor is so small that it can be ignored, perform the following tasks: 2T a s...
The
following elementary gas phase reaction
A+2B—>C+D
Feed is A/B= 1/3 mol A/I =4/1 (mole basis)
is to be carried out in an isothermal CSTR. Given that:
T=500C
P=5 atm
Ea=15500cal/gmol
A=1.5e4
K=A*exp^(-Ea/RT)
Qo= 100 L/s
Reactor volume= 20,000L
a) what are the exit molar flow rates? Fa, Fb, Fc, Fd,
Fi
b) what is the exit volumetric flow rate Q?
2. The following elementary irreversible gas-phase reaction: A+2B >C+D Is to carried out in an isothermal CSTR. Given that:...
Question 5 (8 Marks): The first order irreversible gas phase reaction a- A B is to be carried out in a packed bed reactor with a 1,000 kg of reforming catalyst are packed. The entering pressure is 20 atm and the pressure at the exit of the reactor is 1.0 atm. Calculate the pressure drop parameter. b- Sketch one reactor that is normally used to maximize the selectivity Briefly describe the two terms in the Arrhenius equation C-
Question 5...
2) ZA → B is a gas-phase elementary reaction carried out in a PFR. Conversion of A = 80%. The feed is pure A. What is conversion when the molar feed rate is cut in half?
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...