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Question 2: Data analysis and reactor design The stoichiometry of a non-elementary liquid-phase reaction can be...
The first order elementary reaction: A + B + C was carried out in a constant...
The first order elementary reaction: A + B + C was carried out in a constant volume batch reactor isothermally at 328 K. The concentrations of species A, CA, were recorded as a function of time, as given in the following table. The activation energy Ea=120 kJ/mol. 0.9 6 t (min) CA (mol/dm) 0 20 0.5 17.4 1.5 12.9 2.2 10.5 4 6.2 15.5 8.3 3.5 Based on integral method: b) Process the data using the above table and the...
Question 2 For an isothermal, constant volume batch reactor in which the following reaction is occurring...
Question 2 For an isothermal, constant volume batch reactor in which the following reaction is occurring A - B A laboratory technician measures the rate of reaction of A in a reactor for different concentrations, and obtains the following data: CA 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 1.0 [mol.L' -TA 0.1 0.4 0.9 1.6 2.5 3.6 4.9 6.4 10 (mol.L-min'] The laboratory technician tells you that if you plot - r against (CA) that you get a straight...
. Question 2: The elementary, reversible, organic, liquid-phase reaction is carried out adiabatically in a CSTR...
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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...
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...
6. For the reaction: C2H4Br2 3 KI C2H4+2 KBr + KI3 Initial rate data at 60...
6. For the reaction: C2H4Br2 3 KI C2H4+2 KBr + KI3 Initial rate data at 60 "C are 0.500 0.500 1.50 1.80 7.20 1.80 0.269 1.08 0.807 The rate law is A) rate-kKI B) rate-C2H4Br2l G) rate KI2 D) rate- kKIIC2H4Br2] E) rate kIKIIC2H4Br2 7. Choose the INCORRECT answer. The rate of a chemical reaction: A) usually is increased when the concentration of one of the reactants is increased B) is dependent on temperature C) may be increased by certain...
helpp 3. For the hypothetical reaction A+B → C the following rate data (with and without...
helpp
3. For the hypothetical reaction A+B → C the following rate data (with and without catalyst) were obtained: Rate, M/s Rate, M/s ALM B., Muncatalyzed) (catalyzed) 0.100 0.200 3.51 x 10 7.14 x 10 0.100 0.100 1.75 x 10 7.14 x 10 0.0500 0.200 1.76 x 10 3.57 x 10 0.0500 0.100 8.80 x 10 3.57 x 10 Based on these data: a. Determine the uncatalyzed and catalyzed rate laws for this reaction, and the corresponding rate constants. (16...
The first order elementary reaction: A + B + C was carried out in a constant volume batch reactor isothermally at 328 K. The concentrations of species A, CA, were recorded as a function of time, as given in the following table. The activation energy Ea=120 kJ/mol. 0.9 6 t (min) CA (mol/dm) 0 20 0.5 17.4 1.5 12.9 2.2 10.5 4 6.2 15.5 8.3 3.5 Based on integral method: b) Process the data using the above table and the...
Question 2 For an isothermal, constant volume batch reactor in which the following reaction is occurring A - B A laboratory technician measures the rate of reaction of A in a reactor for different concentrations, and obtains the following data: CA 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 1.0 [mol.L' -TA 0.1 0.4 0.9 1.6 2.5 3.6 4.9 6.4 10 (mol.L-min'] The laboratory technician tells you that if you plot - r against (CA) that you get a straight...
.
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...
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...
6. For the reaction: C2H4Br2 3 KI C2H4+2 KBr + KI3 Initial rate data at 60 "C are 0.500 0.500 1.50 1.80 7.20 1.80 0.269 1.08 0.807 The rate law is A) rate-kKI B) rate-C2H4Br2l G) rate KI2 D) rate- kKIIC2H4Br2] E) rate kIKIIC2H4Br2 7. Choose the INCORRECT answer. The rate of a chemical reaction: A) usually is increased when the concentration of one of the reactants is increased B) is dependent on temperature C) may be increased by certain...
helpp
3. For the hypothetical reaction A+B → C the following rate data (with and without catalyst) were obtained: Rate, M/s Rate, M/s ALM B., Muncatalyzed) (catalyzed) 0.100 0.200 3.51 x 10 7.14 x 10 0.100 0.100 1.75 x 10 7.14 x 10 0.0500 0.200 1.76 x 10 3.57 x 10 0.0500 0.100 8.80 x 10 3.57 x 10 Based on these data: a. Determine the uncatalyzed and catalyzed rate laws for this reaction, and the corresponding rate constants. (16...
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