26. A 2m3 CSTR processes an aqueous feed containing reactant A. This is a second order...
26. A 2m3 CSTR processes an aqueous feed containing reactant A. This is a second order reaction occurring at a constant temperature of 80°C. Calculate the conversion of reactant A in a CSTR. Round your answer to three decimal places. Data: 2A C Qo = 100 L min-1 40 = 100 mol L-1 ra =-0.02 CA2 [mol L-1 min 1]
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...
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?...
An aqueous solution containing reactant A is fed to a batch reactor, operated as part of a continuous process involving other equipment. The feed rate to the reactor is 500 L/min. The reaction, A + 2B rightarrow C is second order irreversible, with the rate expression given as rr_A = 0.04 C_AC_B, gmole/L middot min If C_A0 = 1.7 gmole/L and C_B0 = 3.0 gmole/L, what is the size of the reactor required to obtain an 80% conversion of A?...
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...
acetaldehyde (CH3CHU) in aqueous For the reaction between hydrocyanic acid (HCN) and solution, HCN(A) + CH3CHO(B) - CH2CH(OH)CN the rate law at 25°C and a certain pH is(-ra)=KACACB, where ka=0.210 L mol"min" (see problem 4-6). If the reaction is carried out at steady-state at 25°C in a CSTR, how large a reactor (V/L) is required for 75% conversion of HCN, if the feed concentration is 0.04 mol L-l for each reactant, and the feed rate is 2 L min!?
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...
, e th the reactor? 310 Ibm? 800 Ib,m. What if To 100°F? 500°F? The first-order irreversitte reacti A)B(g) + C(8) is carried out adiabatically in a CSTR into which 100 mol/min of pure liquid A is fed at 400 K. Th e reaction goes virtually to completion i.e., the feed rate e reactor equals the product of reaction rate inside the reactor and the into the reactor volume B(g) C(g) CSTR How many moles of liquid A are in...
The elementary gas phase reaction (A <--> 2B) is to be carried out in an adiabatic CSTR. The feed which is at a temperature of 27oC, consists of 80% of A and the remainder inerts. The volumetric flow rate entering the reactor at this temperature is 100 l/min. The concentration of A in the feed at 27oC is 0.5 mol/liter. For 80% of the adiabatic equilibrium conversion, calculate the required reactor volume. DATA: CpA=12 J/mol.K; CpB=10 J/mol.K; CpI=15 J/mol.K deltaHrxn=-75000...
Using optimum temperature progression in a mixed flow reactor for the reaction between 0 °C and 100 °C A------>R, ∆H298 = −75300 J/mol, ∆G298 = −14130 J/mol, CPA=CPB= constant= 250 cal/mol K, (a) Calculate the size of reactor is needed for 80% conversion when CAO = 4 mol/lit, FAO = 1000 mol/min. (b) What is the heat duty if feed enters at 25 °C and product is to be withdrawn at this temperature? CPA is 250 cal/mol K