1- At present the elementary liquid-phase reaction A + B R + S takes place in a plug flow reactor using equimolar quantities of A and B. Conver- sion is 96%, CAO = CB0 = 1 mol/liter. If a mixed flow reactor ten times as large as the plug flow reactor were hooked up in series with the existing unit, which unit should come first and by what fraction could production be increased for that setup? %3D

1. The reaction A → B is to be carried out isothermally in a continuous-flow reactor. The entering volumetric flow rate (v.) is 8 L/h. For a constant volumetric flow rate v = Do, then FA CAVO Also, CAO FAO/vo. Pure species A enters into the reactor at a rate of 4 mol/h. Calculate both the CSTR and PFR volumes necessary to consume 99% of species A (i.e., CA = 0.01CAo) assuming the reaction rate -гA is a. -TAKA with kA = 0.05 mol/L.h b. rA KACA with kA = 0.0001 s¨¹ C. -TA KA(CA)² with kA = 300 L/mol.h 2. Repeat parts a, b, and c above to calculate the time necessary to consume 99.9% of species A in a 1,000 L constant-volume batch reactor with CA。 = 0.5 mol/L.

note: this is about chemical reaction engineering conversion and reactor sizing. show all the necessary steps and solutions. correct answer only pls. thank you. type the answer.