The biodiesel formation reaction is carried out in a plug flow reactor. Oil is fed at a flowrate of 10 mol/s. Methanol is fed at a flowrate of 30 mol/s. Determine the volume of the reactor required for a conversion of 95%. Assume that the reaction is irreversible and the reaction is first order with respect to both oil and methanol. Assume that the density of the mixture stays constant along the reactor as 5000 mol/m3. The rate constant for this reaction is 1 m3/(mol.s). The design equation for a plug flow reactor is rA=dFA/dV. State all your assumptions.
The biodiesel formation reaction is carried out in a plug flow reactor. Oil is fed at...
3. (15 points): The reaction of is carried out isothermally in a continuous flow reactor. Calculate both the CSTR and the PFR reactor volumes (if it is possible) necessary to consume 96% of S (ie. S-0.04*So) when the entering volumetric flow rate is at a constant 12 L/hr. Assume the reaction rate -rs follows normal Michaelis-Menten kinetics (the product formation step is slow and rate limiting) where the substrate binds with the enzyme to form complex ES. Assume that there...
2. The following reactions are carried out in the liquid phase in a plug flow reactor operating isothermally at steady state. kI A2B and BD. k2 The specific reaction constants are given as k 0.1 sec and k2 0.05 sec. The volumetric flow rate to the reactor is F 5 m/nia and the inlet concentrations of A, B and D are: C 2 kmol/m', CoO kmol/m', and Coo0 kmo/m a). What is the value of Ca at the exit of...
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)
QUESTION 5 The following gas-phase reaction takes place in a plug flow reactor (a tubular reactor) that has a diameter of 6 inches and cross sectional area of 0.1 ft2. A C.The reaction rate depends only on the concentration of A, CA, and has the following form: rate of destruction of A-k * CA , where k= 0.124 s-1. The feed consists of pure A, and enters the reactor at a volumetric flowrate of 0.22 ft3/s. Determine the required length...
PROBLEM 1 The elementary liquid phase irreversible reaction (A + B -> C) is to be carried out in a flow reactor. An equimolar feed with A and B enters the reactor at 300K at a volumetric flow rate of 2 L/s, and feed molar concentration of A equal to 0.1 kmol/m3 a. A. Calculate the conversion of A that can be achieved in one 500 Liter Mixed Flow Reactor under adiabatic conditions. b. Calculate the conversion of A that...
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 elementary irreversible organic liquid-phase reaction. a+b==>c is carried out adiabatically in a flow reactor. An equal molar feed in A and 8 enters at 27'C, and the volumetric flow rate is 2 dm3/sa nd CAo= 0.I k molfm3 graphically.on exal
The production of methyl bromide is an irreversible liquid-phase reaction that follows an elementary rate law. The reaction CNBr (A) + CH3NH2 (B)àCH3Br (C) + NCNH2 (D) is carried out isothermally in a semi-batch reactor. A solution of methylamine (B) in extra dry ethanol at a concentration of 0.025 mol/L is to be fed at a rate of 0.05 L/s to an solution of bromine cyanide (A) in extra dry ethanol contained in a glass-lined reactor. The initial volume of...
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...
The elementary, reversible gas phase reaction A B is to be carried out in a CSTR with heat exchange. Pure A is fed to the reactor. The heat exchange coil in the reactor is maintained at 400K. The rate coefficient is known at 400K, but heat of reaction is unknown. Data: k1(400K) = 0.001 s.! V-1000L To=350K R-831 J/mol K h 5 mol's UA 1000 J/K Kea (450K-1 A) Calculate the conversion (X) if the steady state CSTR is operated...