Aqueous feed containing reactant A (CA0=2 mol/L) enters a plug flow reactor (10L)which has a provision for recyclying a portion of the flowing stream. The reaction kinetics and stoichiometry are: A R -rA=1CACR(mol/L-min) and we wish to get 96% conversion. At what value should we set the recycle flow rate so as to obtain the highest production

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 …

Question: 6075.13 Question 5 10 pts lf k , , and CA0 are constants equal, respectively, to 2.0, 2.3, and 20, The parameter X varies from an initial value 0 to a final value of 0.76, what is the value of V given the following equations and assuming that the integral of dV equals V: CA =C40 (1-X) A change of variables from dCA to dX is helpful.

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.

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.

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.

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

Question: La reacción orgánica irreversible elemental en fase líquida. A + B --> C se lleva a cabo adiabáticamente en un reactor de flujo. Una alimentación molar igual en A y B entra a 27 °C, y el caudal volumétrico es de 2 dm3/s y cA0 = 0,1 kmol/m3.

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.

The first-order reversible liquid reaction A⇌R, CA0=0.5 mol/liter, CR0=0 takes place in a batch reactor. After 8 minutes, conversion of A is 33.3% while equilibrium conversion is 66.7%. Find the rate equation for this reaction.