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An irreversible first order reaction is being .5 carried out in a CSTR and PFR of...
The first order irreversible reaction A -> B is carried out in a CSTR. The rate...
The first order irreversible reaction A -> B is carried out in a CSTR. The rate constant is 0.05 s^-1 and the volumetric flowrate is 0.02 m^3 s^-1. What volume of reactor is required in order to achieve a conversion of 80%? Hint:(Conversation of Ca to molar flowrate/volumetric flowrate)
An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second...
An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second order in A. The feed is equimolar A and solvent (S, which contains catalyst), and enters the reactor at a total volumetric flow rate of 10 dm3/min at a concentration of A of 4 mol/L. The feed enters at 300 K. The product and reactant heat capacities are 15 cal/(mol°C), the solvent is 18 cal/(mol°C). The reaction rate constant at 300 K...
(1) Which system has higher conversion for a 2nd order isothermal reaction? CSTR PFR B PFR...
(1) Which system has higher conversion for a 2nd order isothermal reaction? CSTR PFR B PFR CSTR C. Same for both D. Need more information to determine.
1. Consider the following irreversible, zero-order, liquid-phase reaction: A ➝ B. The reaction is strongly exothermic,...
1. Consider the following irreversible, zero-order, liquid-phase reaction: A ➝ B. The reaction is strongly exothermic, or ∆???? ? ≪ 0. For a given conversion XA, would an adiabatic CSTR and an adiabatic PFR require the same volume? If not, which reactor requires less volume? Justify your answer physically.
Question 1: Design of isothermal reactors 30 Marks The irreversible, gas-phase reaction A+B D is to be carried out...
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...
Please answer all parts 2. A total of 10000 L/h of metaxylene, C&H(CHs)2, is being isomerized...
Please answer all parts
2. A total of 10000 L/h of metaxylene, C&H(CHs)2, is being isomerized to a mixture of orthoxylene, metaxylene, and paraxylene in a reactor with a volume of 1000 L. The isomerization reaction can be represented as: where A is the metaxylene being fed to the reactor, and B are the different isomers formed. The reaction is being carried out at 400°C and 20 bar. Under these conditions, 35% of the metaxylene fed to the reactor is...
Reaction is A-->B is carried out adiabatically in a CSTR. The reaction is second order in...
Reaction is A-->B
is carried out adiabatically in a CSTR. The reaction is second order in A. The feed, which is equal molar in water (which contains the catalyst) and A, enters the reactor at a temperature of 52 C and a total volumetric flow rate of 10 dm3/min. The concentration of A entering the reactor is 4 molar. a) What is the reactor volume to achieve 80% conversion b) What conversion can be achieved in a 1000 dm3 CSTR?...
The first order reaction A rightarrow B is carried out in an adiabatic CSTR with A_A0...
The first order reaction A rightarrow B is carried out in an adiabatic CSTR with A_A0 = 2 mol/liter and T_0 = 300 degree K. It is found that 50% conversion is obtained with tau (=V/Q) = 4 min, and the reactor temperature is 350 degree K. The reaction rate constant k at 350 degree K is The reaction is in water with rho_C_p = 1000 cal/liter degree K. Find the heat of reaction.
. Question 2: The elementary, reversible, organic, liquid-phase reaction is carried out adiabatically in a CSTR...
.
Question 2: The elementary, reversible, organic, liquid-phase reaction is carried out adiabatically in a CSTR where 65% conversion is achiewd Ated'anonn of A and 50% excess 8, enters the reactor at 27°C with a volumetric flow rate of 2 L/s and a Cos of O.1 mol/L culate the temperature inside the reactor 2. Calculate the equilibrium conversion at the operating temperature. How close (in 3. Calculate the CSTR volume percentage) the conversion is from the equilsbrium conversion? If the...
2. The irreversible gas phase reaction A B is carried out isothermally in a fluidized catalytic...
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...
An acid-catalyzed irreversible liquid-phase reaction A B is carried out adiabatically in a CSTR. The reaction is second order in A. The feed is equimolar A and solvent (S, which contains catalyst), and enters the reactor at a total volumetric flow rate of 10 dm3/min at a concentration of A of 4 mol/L. The feed enters at 300 K. The product and reactant heat capacities are 15 cal/(mol°C), the solvent is 18 cal/(mol°C). The reaction rate constant at 300 K...
(1) Which system has higher conversion for a 2nd order isothermal reaction? CSTR PFR B PFR CSTR C. Same for both D. Need more information to determine.
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...
Please answer all parts
2. A total of 10000 L/h of metaxylene, C&H(CHs)2, is being isomerized to a mixture of orthoxylene, metaxylene, and paraxylene in a reactor with a volume of 1000 L. The isomerization reaction can be represented as: where A is the metaxylene being fed to the reactor, and B are the different isomers formed. The reaction is being carried out at 400°C and 20 bar. Under these conditions, 35% of the metaxylene fed to the reactor is...
Reaction is A-->B
is carried out adiabatically in a CSTR. The reaction is second order in A. The feed, which is equal molar in water (which contains the catalyst) and A, enters the reactor at a temperature of 52 C and a total volumetric flow rate of 10 dm3/min. The concentration of A entering the reactor is 4 molar. a) What is the reactor volume to achieve 80% conversion b) What conversion can be achieved in a 1000 dm3 CSTR?...
The first order reaction A rightarrow B is carried out in an adiabatic CSTR with A_A0 = 2 mol/liter and T_0 = 300 degree K. It is found that 50% conversion is obtained with tau (=V/Q) = 4 min, and the reactor temperature is 350 degree K. The reaction rate constant k at 350 degree K is The reaction is in water with rho_C_p = 1000 cal/liter degree K. Find the heat of reaction.
.
Question 2: The elementary, reversible, organic, liquid-phase reaction is carried out adiabatically in a CSTR where 65% conversion is achiewd Ated'anonn of A and 50% excess 8, enters the reactor at 27°C with a volumetric flow rate of 2 L/s and a Cos of O.1 mol/L culate the temperature inside the reactor 2. Calculate the equilibrium conversion at the operating temperature. How close (in 3. Calculate the CSTR volume percentage) the conversion is from the equilsbrium conversion? If the...
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...
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