Problem 2 Consider an exothermic reactie occurring in a batch reactor, as shown in the figure. The reaction mechanism is first order reaction Bath Anhiens reaction rate law applies n =kCA = kye-E/RTCA Org GOT Write the model equations of the system as a c

匿名用户 最后更新于 2021-12-01 18:55 其他 All Others


Problem 2 Consider an exothermic reactie occurring in a batch reactor, as shown in the figure. The reaction mechanism is first order reaction Bath Anhiens reaction rate law applies n =kCA = kye-E/RTCA Org GOT Write the model equations of the system as a constant volume system, solve the sets of differential equations using the ODE Sanciots in MATLAB or using the Runge-Kutta 4 order method Pick the stepsise that will ensure high accuracy The following information are provided The volume of the vessel is 10 m The density of the liquid inside the reactor pok The pre exponential factor in Amharious solution is es The heat capacity of the floud is! The heat transfer coefficient U - 1001mc The heat transfer arca A-10m The activation energy E-29 j'mele Heat of reaction is-700kj mele The initial temperature inside the teachers Cad the initial concentration is 0.5 molem The surrounding temperature is 35C Plot the behaviour of the concnetration and the temperature If the initial conenetration was changed from 0 to 2 molem how the temperature inside the reactor will change comment on the real Problem 2 Consider an exothermic reaction occurring in a batch reactor, as shown in the figure. The reaction mechanism is first order reaction A+ B, and the Arrhenius reaction rate law applies n = kCA = koe-E/RT CA Out V T. GCT Write the model equations of the system assuming a constant volume system, solve the sets of differential equations using the ODE funcions in MATLAB or using the Runge-Kutta 4th order method. Pick the step size that will ensure high accurasy The following information are provided The volume of the vessel is 10 m The density of the liquid inside the reactor p=800kg/m The pre exponential factor ko in Arrehnious relation is 0.5 The heat capacity of the flouid is 1 J/c The heat transfer coefficient U = 100 J/s mc The heat transfer area A=10m The activation energy E -20 j/mole Heat of reaction is - 700 kj/mole The initial temperature inside the reactor is 20C and the initial concentration is 0.5 mole /m? The surrounding temperature is 35C. Plot the behaviour of the concnetration and the temperature If the initial concnetration was changed from 0.5 to 2 mole/m, how the temperature inside the reactor will change? comment on the results

已邀请: