Question
A factory is working on the production of U substance. Production will be carried out in a continuous stirring reactor (CSTR) with a LIQUID phase
A factory is working on the production of U substance. Production will be carried out in a continuous stirring reactor (CSTR) with a LIQUID phase reaction. The enthalpy of the reaction taking place in the form of A U (-AH) is 51 kcal/mol, the reaction rate model is known as - 4.3x10e-Ea/RT CA kmol/m's. Pure A component will be fed to the reactor at 35 C, at a concentration of 3.2 kmol/m3 and at a flow rate of 0.06 m3 per second. Calculate the conversion to be achieved and the temperature to be reached if the reactor with a volume of 19 tons is operated adiabatically, with the help of the following data. Cp-4.18j/gK P=980 kg/m3 EA=15700 cal/mol
Bir fabrikada maddesinin retimi zerine allmaktadr. Uretim srekli karmal bir reaktrde (CSTR) srv faz tepkimesi ile gerekletirilecektir. A eklinde gerekleen tepkimenin entalpisi (H)51kcal/mol, tepkime hz modeli rA=4,3106ea/RTCAkmol/m3s olarak bilinmektedir. Reaktre 35C de, 3,2kmolm3 deriimde ve saniyede 0.06m3 ak hznda saf A bileeni beslemesi yaplacaktir. 19 ton hacmindeki reaktr adyabatik olarak iletilirse elde edilecek dnuuum ve ulalacak scakl aadaki veriler yardmryla hesaplayiniz. Cp=4.18j/gKP=980kgm3EA=15700cal/mol Bir fabrikada maddesinin retimi zerine allmaktadr. Uretim srekli karmal bir reaktrde (CSTR) srv faz tepkimesi ile gerekletirilecektir. A eklinde gerekleen tepkimenin entalpisi (H)51kcal/mol, tepkime hz modeli rA=4,3106ea/RTCAkmol/m3s olarak bilinmektedir. Reaktre 35C de, 3,2kmolm3 deriimde ve saniyede 0.06m3 ak hznda saf A bileeni beslemesi yaplacaktir. 19 ton hacmindeki reaktr adyabatik olarak iletilirse elde edilecek dnuuum ve ulalacak scakl aadaki veriler yardmryla hesaplayiniz. Cp=4.18j/gKP=980kgm3EA=15700cal/molStep by Step Solution
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