I need answers for those questions

Consider a liquid phase reaction that occurs in a PFR: a A + B + C The reaction is first order with the following rate expression: 1 (-A) = KCA k = 1x1012 exp -160010 RgT S The reactor is 100 cm long and 5 cm in diameter. The volumetric flow rate of the feed is 1 Litre/s at a temperature of 670 K. The concentration of A in the feed is 1 mol/Litre. The density of the liquid (constant) is 1000 kg/m and the heat capacity of stream (assume constant) is 1000 J kg K kJ The enthalpy change of reaction (assume constant) is -190 The overall heat transfer mol W coefficient (constant) is 1000 For parts (c) and (d) below, the heat transfer fluid has a mass mK J flow rate of 0.1 kg/s and the heat capacity is a constant 1000 kg. K (a) Calculate and plot the reactor temperature profile for adiabatic operation. (b) Calculate and plot the reactor temperature profile for operation with a constant temperature heat transfer fluid at 273 K. (c) Compute and plot the temperature profiles of the process stream and the heat transfer fluid for non-adiabatic operation when the heat transfer fluid enters at 200 K and flows in co-current flow with the process stream. (d) Repeat part (c) but with counter current flow. (e) If the temperature of the heat transfer fluid is held constant at 273 K, determine what the feed inlet temperature should be to have exactly 95% conversion at the reactor exit