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P25.7 The composition of a liquid-phase reaction 2A-> B was followed by a spectrophotometric method with...
The irreversible, endothermic, elementary, liquid-phase reaction: 2A ---> B, is carried out adiabatically in a 100 li...
The irreversible, endothermic, elementary, liquid-phase reaction: 2A ---> B, is carried out adiabatically in a 100 liter PRF. Species A and inert liquid are fed to the reactor with concentrations CAo = 1.5 mol/l and CIo = 1.5 mol/l, while FAo=20 mol/min. The entering temperature is 400 K. Calculate the conversion and temperature at the exit of the reactor, given the additional information below: k = 0.0003 l/(mol*min) at 300 K E= 12000 cal/(mol* K) CpA = 10 cal/(mol*K), CpB...
The reversible liquid reaction 2A ↔ B + C is carried out in an isothermal CSTR...
The reversible liquid reaction 2A ↔ B + C is carried out in an isothermal CSTR with no pressure drop. The feed has an A concentration of 0.1 lbmol/ft3 and T=300K. The forward reaction rate constant is 1800 ft3/lbmol-s and the concentration equilibrium constant is 0.3. a. Determine the equilibrium conversion. b. Determine the reactor volume necessary to achieve 98% of the equilibrium conversion of A if the feed is 10 lb mol/min.
QUESTION 9 Initial rate, mol/L.s Given the data below for the reaction, 2A + 2B +...
QUESTION 9 Initial rate, mol/L.s Given the data below for the reaction, 2A + 2B + 4C => D + E +3 F Experiment Initial conc of A Initial conc of B. Initial conc of C, mol/L mol/L mol/L 0.1 0.1 0.2 0.3 0.3 0.4 N 0.2 2 x 10-3 4x 10-3 6 x 103 8x10-3 w A Calculate the value of k to 3 significant figures. QUESTION 7 For the reaction, 2 A(g) + 2 B(g) => C(g) +...
Reactions Engineering. Please answer fully with explanation and write neatly. Thanks xx Question 3 (20 marks, 36 minutes) Substance A in the liquid phase produces R and S by the following reaction...
Reactions Engineering. Please answer fully with
explanation and write neatly. Thanks xx
Question 3 (20 marks, 36 minutes) Substance A in the liquid phase produces R and S by the following reactions: R RCA The feed (CA,-ו0. CR0-0, Cs,-0.3 miol/ dm) enters two mixed flow reactors in series (τ min, T 10 min). 2.5 Knowing the composition in the first reactor (CA composition leaving the second reactor 0.4, C'R-0.2, C's 0.7 mol/ dm), find the 118] 32 What is the...
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...
PROBLEM 2 The elementary liquid phase irreversible reaction (A+B -> C) takes place in a 1...
PROBLEM 2 The elementary liquid phase irreversible reaction (A+B -> C) takes place in a 1 m² Mixed Flow Reactor with the equimolar mixture of A and B at the volumetric feed flow rate of 0.5 m3/min, the feed concentration of A equal to 1 mol/L, and the feed temperature of 300K. When the reaction takes place under isothermal conditions at 300K the conversion of A is 30%. When the reaction takes place adiabatically the exit temperature is 350K and...
5.33. When B is mixed with A, the liquid phase reaction A+BC rkCA has a rate...
5.33. When B is mixed with A, the liquid phase reaction A+BC rkCA has a rate constant k 0.2 min. This reaction is to be carried out isothermally in a CSTR at steady state. The reactant A costs $2/mol and reactant B costs $0.10/mol. The product C sells for $6/mol. The cost of operating the reactor is $0.05 per liter per hour. We wish to produce 360,000 moles of C per day to meet the market demands The available reactants,...
An exothermic elementary reversible isomerisation reaction of A B in liquid phase is carried out adiabatically...
An exothermic elementary reversible isomerisation reaction of A B in liquid phase is carried out adiabatically in a CSTR. Pure A is fed to the reactor at a concentration of 5 mollitre and feed rate of 500 mol/min. As a researcher you need to analyze the effect of different inlet temperature to the rate of reaction. The inlet temperature is varied at 50°C, 100°C and another two inlets temperature in between 70°C to 90°C. Perform your calculation based on energy...
For the reaction of 2A ---> B + C, the following data are obtained for [A]...
For the reaction of 2A ---> B + C, the following data are obtained for [A] as a function of time time (min) [A] (mol L-1) 0 0.80 8 0.60 24 0.35 40 0.20 a). Determine the order and the rate law of the reaction. (Hint: Consider the integrated rate laws shown on the first page). b). Calculate the value of the rate constant k
Consider an isothermal CSTR, with the liquid phase inlet feed of: Fao 61 mol/hr benzene Vo 10 L/m...
Consider an isothermal CSTR, with the liquid phase inlet feed of: Fao 61 mol/hr benzene Vo 10 L/min Diphenyl is synthesized by the following irreversible reaction 2benzene-» diphenyl H2 with the rate law: Tbenzene-kCbenzenek 0.2 L/(mol'min) a. Wirite the stoichiometric table for this reaction. b. What volume CSTR is required for the exit concentration of benzene to be 12 mM? c. What is the extent of reaction? d. What is the conversion of benzene?
Consider an isothermal CSTR, with the...
QUESTION 9 Initial rate, mol/L.s Given the data below for the reaction, 2A + 2B + 4C => D + E +3 F Experiment Initial conc of A Initial conc of B. Initial conc of C, mol/L mol/L mol/L 0.1 0.1 0.2 0.3 0.3 0.4 N 0.2 2 x 10-3 4x 10-3 6 x 103 8x10-3 w A Calculate the value of k to 3 significant figures. QUESTION 7 For the reaction, 2 A(g) + 2 B(g) => C(g) +...
Reactions Engineering. Please answer fully with
explanation and write neatly. Thanks xx
Question 3 (20 marks, 36 minutes) Substance A in the liquid phase produces R and S by the following reactions: R RCA The feed (CA,-ו0. CR0-0, Cs,-0.3 miol/ dm) enters two mixed flow reactors in series (τ min, T 10 min). 2.5 Knowing the composition in the first reactor (CA composition leaving the second reactor 0.4, C'R-0.2, C's 0.7 mol/ dm), find the 118] 32 What is the...
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...
PROBLEM 2 The elementary liquid phase irreversible reaction (A+B -> C) takes place in a 1 m² Mixed Flow Reactor with the equimolar mixture of A and B at the volumetric feed flow rate of 0.5 m3/min, the feed concentration of A equal to 1 mol/L, and the feed temperature of 300K. When the reaction takes place under isothermal conditions at 300K the conversion of A is 30%. When the reaction takes place adiabatically the exit temperature is 350K and...
5.33. When B is mixed with A, the liquid phase reaction A+BC rkCA has a rate constant k 0.2 min. This reaction is to be carried out isothermally in a CSTR at steady state. The reactant A costs $2/mol and reactant B costs $0.10/mol. The product C sells for $6/mol. The cost of operating the reactor is $0.05 per liter per hour. We wish to produce 360,000 moles of C per day to meet the market demands The available reactants,...
An exothermic elementary reversible isomerisation reaction of A B in liquid phase is carried out adiabatically in a CSTR. Pure A is fed to the reactor at a concentration of 5 mollitre and feed rate of 500 mol/min. As a researcher you need to analyze the effect of different inlet temperature to the rate of reaction. The inlet temperature is varied at 50°C, 100°C and another two inlets temperature in between 70°C to 90°C. Perform your calculation based on energy...
Consider an isothermal CSTR, with the liquid phase inlet feed of: Fao 61 mol/hr benzene Vo 10 L/min Diphenyl is synthesized by the following irreversible reaction 2benzene-» diphenyl H2 with the rate law: Tbenzene-kCbenzenek 0.2 L/(mol'min) a. Wirite the stoichiometric table for this reaction. b. What volume CSTR is required for the exit concentration of benzene to be 12 mM? c. What is the extent of reaction? d. What is the conversion of benzene?
Consider an isothermal CSTR, with the...
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