acl bi zm lazm bu iki soruyu

1) Ideal process Akish In a Larstymall took type reactor (CSTR), the conversion values obtained for 24+3R liquid parse reaction in the fork-fed dobiler per second of residence in the reactor are given in the table below. Initial Concentration of the substance is 25 mollm 3 tor. The same reaction ish A concentration of 25mol/m ? decrease from its value to 10mol/m3 in the isih piston alasti reactor What should be the length of stay? 2) In the verbal phase of the A+BL reaction, the volumes of back-mixing aqueducts with volumes of 100 and 200 liters are greatly affected by this A'mg malar flow rate fed to the 1 st reactor is 10mol/min and the change of A concentration in samasta is given below. .2. reater Calculate 's mob flow when stuck. (Graphic method kelloarak) 1) Ideal process Akish In a Larstymall took type reactor (CSTR), the conversion values obtained for 24+3R liquid parse reaction in the fork-fed dobiler per second of residence in the reactor are given in the table below. Initial Concentration of the substance is 25 mollm 3 tor. The same reaction ish A concentration of 25mol/m ? decrease from its value to 10mol/m3 in the isih piston alasti reactor What should be the length of stay? 2) In the verbal phase of the A+BL reaction, the volumes of back-mixing aqueducts with volumes of 100 and 200 liters are greatly affected by this A'mg malar flow rate fed to the 1 st reactor is 10mol/min and the change of A concentration in samasta is given below. .2. reater Calculate 's mob flow when stuck. (Graphic method kelloarak)