Question

Question 2: The elementary, reversible, organic, liquid-phase reaction is carried out adiabatically in a CSTR where 65% conversion is achiewd Ated'anonn of A and 50% excess 8, enters the reactor at 27°C with a volumetric flow rate of 2 L/s and a Cos of O.1 mol/L culate the temperature inside the reactor 2. Calculate the equilibrium conversion at the operating temperature. How close (in 3. Calculate the CSTR volume percentage) the conversion is from the equilsbrium conversion? If the reactor is to be operated isotherrmally, calculate the rate at which heat need to be removed and the required heat exchanger area (Ur 10 cal/m2.s-K, T,-290 K. c 18 cal/molk). -8 5. Suppose that the reaction was A → C, the reactor was a PFR with heat exchanger, and the feed was pure A. Differentiate the algebralc energy balance equation with respect to volume to obtain an equation for dTid respect to volume to obtain an equation for Tldv erties, kinetic and thermedynemic datoa Coa 15 cal/(mol K) Cos 15 cal/(mol K) Cpc 15 cal/(mol K) 4m-6 kcal/mol at 298 K k 0.01 L/mol-s at 300 K E = 10,000 cal/mol K 50 at 373 K

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Answer 1

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