the order of system is 2 since the highest exponent of s is 2
Problem: A reaction A+ R takes place in a constant-volume isothermal CSTR. The component mass balances...
2. A first order reaction ( - A = kC ) takes place in an isothermal trickle bed reactor with volume of V which is shown in figure below. There is an agitator in the reactor to provide uniform mixing. Reactants and products are pumped to another pipeline with a centrifugal pump. At the pump outlet, a portion of the stream is sent to the reactor as a recycle. By performing unsteady state and steady state material balances, find the...
Fo, Co RF_C2 0 V V F1C1 F2, C₂ Figure above show isothermal reactors where both reactor having a first order reaction A -> B with rate reaction constant k. Volume of reactors, V = 4m3 are constant and equal; the flow rate FR = 2 m3/hr and the recycle ratio R = 3 are constant. Include your assumptions. The mathematical models of this process for the deviation variables are developed as below: 4 dc' | 2 co + 6...
3. Steady-State CSTR Assume you have an adiabatic CSTR operating at steady-state. Within the CSTR, reactant A is being converted to product, where the rate of reaction is first order: A =kC However, the reaction is also exothermie, and the rate constant is described through the classic Arrhenius equation: k(T) = k e RT Under the set of conditions given, solve for the temperature (T) and the concentration (CA) leaving this CSTR operating under steady-state conditions. k . CA0| 3000...
please solve it right . Example: Van de Vusse Reaction in an CSTR Van de Vusse liquid phase reaction is carried out in an isothermal CSTR according to the following stoichiometric equations: k3 where B is the desired product, and C and D are the undesired byproducts. The feed to the CSTR contains the reactant A only. The reaction rates are given by the following rate laws: 2 Additional information: k 0.8333 min k2 1.667 min, k3 0.1667 L min...
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) Consider the stirred tank reactor under isothermal conditions. The reaction occurring is 7 A → P and it proceeds at a rate TA=-k.CA/(1+k2.C); mole/m.h ki = 1.0 h k2 -1.0 m/mole Data: V = 2 m'; F = 1 m/h; CA (0) -0.5 mole/m Assuming constant density and volume, derive the transfer function relating the concentration in the reactor to the feed stream concentration. Analytically obtain the response of reactor concentration to a unit step change in CAO (10...
2 of 6 04-Chem-A4/Dec 2012 1. A first-order, homogeneous, liquid-phase reaction (A - B) occurs in a CSTR that operates adiabatically at steady state. The reaction is exothermic. Data are as follows and should be considered as exact quantities CA G, 1.75 molA/L (Inlet concentration of A) 2.5 J/g-K (The heat capacity of the reacting fluid; assumed constant at all conversions.) AH, -27 000 J/molA q-30 L/min (Flow into the CSTR.) (-rA) = 1.8( 1013)e(-84000 RDCA (The rate of reaction...
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...
The irreversible reaction A+B -C takes place isothermally and with no volume change. The kinetic rate expression follows that of an elementary reaction. Make plots of the ratio of the radius, Re, of a spherical CSTR to the length, L, of a cylindrical plug flow reactor of constant cross section of radius Rp as a function of conversion, when the ratio Re /Rp varies from 1 to 10. The feed to the reactors is an equimolar mixture of A and...
by using MATLAB answer is Code Component A reacts irreversibly and at a specific reaction rate k to form product, component B via the first order reaction A as shown in figure 2 B in a three CSTRs connected in series Let the concentration of component A in the inflowing feed stream be Co. (kmoles of A per unit volume) and in the reactor CA. The resulting govering equations are given below decat (C0CH) -RCHI den (C1-C12) -kCz2 des C12-602)...