2A → B+C is carried out in the flow reactor under isothermal and isobaric condition. The specific reaction rate at 325 K is 10 min and the activation energy is 95 kJ/mol. Pure A enters the reactor at 10 atm and 500 K and a molar flow rate of 50 mol/min. Calculate the reactor volume to achieve 60% conversion in a Plug Flow Reactor (PFR). (a) If a CSTR is placed after the PFR to increase the conversion to 80%, as shown in Figure Q1(b), calculate the Continuous Stirred Tank Reactor (CSTR) volume for the reactors system. (b)

Please help me with this one as soon as you can and show all the work for the enthalpy table. I provided the problem statement and the enthalpy table I need filled out please show the work for it.

Product B is produced in a batch reactor according to the elemental reversible reaction (A⇋B) in liquid phase. The reactor volume is 10 L and the reaction temperature is 60°C. The initial concentration of reagent A is 3 lbmol/L, the rate constant for the forward reaction is k1=6.0 h-1, and the rate constant for the reverse reaction is k2=0.53h-1. Determine: (a) Plot the concentration of each species as a function of reaction time(b) Plot the conversion as a function of reaction time

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gas phase reactionA -> B + Ccarried out isothermally in a constant volume batch reactor of 100 L. An amount of 100 moles of pure A is initially placed in the reactor. The reactor is well mixed and the ideal gas equation holds. If the reaction is first order,-rA = kCA with k = 1 1/sCalculate the time required to consume 80% (moles) of A.

The elementary reversible gas phase reaction A+ 2B is to be carried out isothermally (250 °C) and at constant pressure in a variable batch reactor. Initially pure A is present at a concentration of 0.01 mol/dm'. Set up the equation (all constant values and limits shown) to solve for the time it will take to reach 85% of the equilibrium conversion of A at 250 °C. T (°C) k (min"') Kc (mol/dm) 200 0.27 0.018 400 1.05 0.006

The following reaction takes place in a catalytic reactor: NO2+O2 → NO3 In the process 1000 mol/s of NO3 are produced. The reaction has 90% conversion and air with 20% excess is supplied. Calculate the flow rates of the system.

DRAW 2D DIAGRAM OF A SOLUTION TO  MAKE THE MIXING MUCH MORE EFFICIENT A first order irreversible reaction is conducted in an 800 L continuously stirred tank, in liquid solution at 80 ᵒC temperature. The total conversion in the tank is calculated to be 60%. However, this conversion appears low.After a quick check, you realise that something in the mixing is not working correctly and as a result, the tank is not optimally stirred. Following a few tests on residence times, you calculate that approximately 300 L of the tank do not interact appreciably with the input or output streams. You therefore decide to modify the reactor by improving the stirring performance in order to obtain complete mixing in the reactor volume. Describe what considerations allowed you to evaluate the ‘unused’ volume in the tank and defend your proposed solution in a brief technical report to be presented to your manager for approval. The report must include a clear schematic drawing of your selected solution

Please don't use hend raiting and step by step solutions

5. [ , The isothermal and isobaric gas phase reaction: A → 2B follows an elementary rate law. The rate constant k = 1.5 s' when the reaction temperature is at T = 350 K. Pure A is fed into a continuous-stirred tank reactor (CSTR) at a volumetric flow rate of 5 dm/s. What conversion of A can the reactor achieve if the reactor has a volume of 20 dm?