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Question: A plug flow reactor (2 m3) processes an aqueous feed (100 liter/min) containing reactant A (CAo = 100 mmol/liter). This reaction is reversible and represented by: a=b rA= 0.04min-1 Ca - 0.01min-1 Cb 1.Find the equilibrium conversion 2.Find the actual conversion of A in the reactor. 3.We wish to achieve 97.5% of the equilibrium ...
Calculations show that a plug flow reactor would give 99.9% conversion of reactant which is in aqueous solution. However, our rector has an RTD somewhat as shown in Fig. P13.13. If Cao = 1000, what outlet concentration can we expect in our reactor if reaction is first order?
Question: 2. In an isothermal batch reactor 70 % of a liquid reactant is converted in 13 min. What space-time and space-velocity are needed to effect this conversion in a plug flow reactor and in a mixed flow reactor?
Question: Consider a gas-phase reaction 2A →R+ 2S with unknown kinetics. If a space velocity of 1/min is needed for 90% conversion of A in a plug flow reactor, find the corresponding space-time and mean residence time or holding time of fluid in the plug flow reactor.
3.6 A plug-flow reactor has a conversion of A of 90%, and the reaction is first order. If a dispersed plug-flow reactor has the same volume and has a dispersion number, D / νL, of 1.0, what will be the percent conversion? Plug-Flow Reactors for a First-Order Reaction of the Type A → Products
A stream of pure gaseous reactant A (CAo = 660 mmol/liter) enters a plug flow reactor at a flow rate of FAo = 540 mmol/min and polymerizes there as follows mmol 3A----->R, -rA=54 mmol/liter.min. How large a reactor is needed to lower the concentration of A in the exit stream to CAf = 330 mmol/liter?
Question: For the reaction of Problem 5.21, what size of plug flow reactor would be needed for 80% conversion of a feed stream of 1000 mol A/hr at CAO 1.5 mol/liter?
Question: The following reaction is carried out in a multi-stage adiabatic plug flow reactor: A + B ↔ C + DThe feed consists of only A & B and enters the first ...
Consider a plug flow reactor of volume 1 m which gives an aqueous feed rate of 5 lit/sec The kinetics of the reaction A Ris represented as, -=(0.6 min)C-(0.35min )C, Calculate the equilibrium conversion of the above reaction. a) 0.56 b) 0.85 c) 0.63 d) 0.74 er AD
Question: 3) Plug flow reactor including heat exchange. Butadiene and ethylene are reacted to form cyclohexene in a PFR: CH,=CH-CH=CH, + CH, CH, acyclohexene The reaction is irreversible and the kinetics are first order in both butadiene and ethylene.