Question: 5.14. A stream of pure gaseous reactant A (CA0 = 660 mmol/liter) enters a plug flow reactor at a flow rate of FAO 540 mmol/min and polymerizes there as follows 3A →R, - = 54 mmol liter · min How large a reactor is needed to lower the concentration of A in the exit stream to Car = 330 mmol/liter?

Aqueous feed containing reactant A (CA0 = 2 mol/liter) enters a plug flow reactor (10 liter) which has a provision for recycling a portion of the flowing stream. The reaction kinetics and stoichiometry are and we wish to get 96% conversion. Should we use the recycle

Aqueous A at a concentration CA0 = 1 mol/liter is introduced into a batch reactor where it reacts away to form product R according to stoichiometry A → R. The concentration of A in the reactor is monitored at various times, as shown below: 1, min CA, mol/m3 0 100 200 300 400 1000 500 333 250 200 For CAO = 500 mol/m find the conversion of ...

Aqueous feed containing reactant A (CA0 = 2 mol/liter) enters a plug flow reactor (10 liter) which has a provision for recycling a portion of the flowing stream. The reaction kinetics and stoichiometry are A mol R, -ra = 1CACR liter · min and we wish to get 96% conversion.

Question: 4.1. Given a gaseous feed, CA0=100,CB0=200, A+B→R+S,XA=0.8. Find XB,CA,CB.temperature T0 and pressure π0, reacts there, and leaves at T and π. 4.5.

A → R; CA0 = 1 mol / liter The decomposition reaction of component A takes place in a batch reactor. At the end of the first hour of the reaction, 75% conversion is reached and at the end of 2 hours the conversion is completed (100% conversion). Derive the rate expression that describes the kinetics of this reaction.

Under ultraviolet radiation, reactant A of CA0 = 10 kmol/m3 in a liquid process stream (Q = 1 m3/min) decomposes as follows: A —> R r1 = 16CA0.5 kmol/(m3×min) A —> S r2 = 12CA Under ultraviolet radiation, reactant A of C A0 = 10 kmol/m 3 in a liquid process stream ( Q = 1 m 3 /min) decomposes as follows:

3.23 for the decomposition A->R, Ca0 =1 mol/liter, in a batch reactor conversion is 75% after 1hour, and is just complete after 2hours. find a rate equation to represent these kinetics. Question: 3.23 for the decomposition A->R, Ca0 =1 mol/liter, in a batch reactor conversion is 75% after 1hour, and is just complete after 2hours. find a rate ...

Answer to 1/ca-1/ca0=k*t k=reaction rate constant t= time. The solution to your question is given below. I hope your doubt is clear.

A feed of aqueous A (CA0 = 40 mol/m3)enters a reactor, decomposes, and a mixture of A, R, and S leaves. 7.8. Find Cr, and Cs, and tau for Xa = 0.9 in a mixed flow reactor. 7.9. Find Cr and Cs and tau for X,a = 0.9 in a plug flow reactor. 7.10. Find the operating condition (Xa, tau and Cs) which maximizes Cs in a mixed flow reactor. 7.11.