Liquid A decomposes by 1st order kinetics in a batch reactor where 50% of A is converted in a 5- min run. How much longer would it take to reach 75% conversion?

A liquid reactant stream (1 mol/liter) passes through two mixed flow reactors in a series. The concentration of A in the exit of the first reactor is 0.5 mol/liter. Find the concentration in the exit stream of the second reactor. The reaction is second-order with respect to A and V2/V1 = 2. reactor design

Example: consider the shock-heating of air to 2500K and 3atm. Find: 1. The initial nitric oxide formation rate in ppm/s. 2. The amount of nitric oxide formed (in ppm)in 0.25ms. Solution: From table 3.3 Kp=0.0002063

A _____________ reactor approaches a _____________ reactor at infinite recycle Fill in the blanks Choices. (a) completely mixed, plug-flow (b) plug-flow, completely mixed, (c) ideal, steadystate(d) plug-flow, ideal

For each of the endothermic and exothermic reactions, explain which reactor type is optimal for adiabatic operation.

Liquid A decomposes by second-order kinetics, and in a batch reactor, 50% of A is converted in a 5 min run. How much longer would it take to reach 75% conversion?A-10 minB-15 minC-12 minD-7.5 min

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When an exothermic reaction proceeds adiabatically in a mixed flow reactor (MFR), outline and explain the characteristic graph of the energy balance and material balance to show that multiple steady states may exist. Also, explain that among multiple steady states, there is an unstable steady state.

Follows an elementary rate law and is carried out isothermally in a flow system. Theconcentrations of the A and B streams are 2M before mixing. The volumetric flow rate ofeach stream is 5 dm3/min and the entering temperature is 300K. The streams are mixedimmediately before entering. Two reactors are available. One is a 200 dm3 CSTR that canbe heated to 77 °C or cooled to 0 °C, the other is a 800 dm3 PFR operated at 300 K thatcannot be heated or cooled. Note that k = 0.07 dm3/mol min at 300 K and E = 83.7 kJ/mola) Which reactor and what conditions do you recommend? Explain the reason of yourchoice (space available, operational complexity). Back up your reasoning with theappropriate calculations b) How long would it take to achieve 90% conversion in a 200 dm3 batch reactor withinitial concentrations CA0 = CB0 = 1M after mixing at a temperature of 77 °C?