first order decay reacti ler CFSTRS that are ope er) reduces the overall m tion efficiency is greate ld improve the efficienc C= 100 mg/L of a reac stant of 0.1 min ¹. Assu that it can be operated es with the detention ti

Materials Science And Engineering Properties
1st Edition
ISBN:9781111988609
Author:Charles Gilmore
Publisher:Charles Gilmore
Chapter4: Temperature Effects On Atom Arrangements And Atom Motion
Section: Chapter Questions
Problem 4.12P
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3. A first order decay reaction is occurring in a single CFSTR. Dividing the reactor into two
smaller CFSTRs that are operated in series (effluent from one serving as the influent to the
other) reduces the overall mixing and therefore makes the flow more PFR-like. Because
reaction efficiency is greater in a PFR than a CFSTR, we might expect that dividing the reactor
would improve the efficiency. To test that hypothesis, consider a system receiving an influent
with C = 100 mg/L of a reactant that undergoes a first order decay reaction with a rate
constant of 0.1 min ¹. Assume that the system has a total hydraulic detention time of 1 hour,
but that it can be operated in three different ways: as a PFR, a CFSTR, or as two CFSTRs in
series with the detention time split equally between the two. Find the effluent concentrations
for the three possible operating modes
Transcribed Image Text:3. A first order decay reaction is occurring in a single CFSTR. Dividing the reactor into two smaller CFSTRs that are operated in series (effluent from one serving as the influent to the other) reduces the overall mixing and therefore makes the flow more PFR-like. Because reaction efficiency is greater in a PFR than a CFSTR, we might expect that dividing the reactor would improve the efficiency. To test that hypothesis, consider a system receiving an influent with C = 100 mg/L of a reactant that undergoes a first order decay reaction with a rate constant of 0.1 min ¹. Assume that the system has a total hydraulic detention time of 1 hour, but that it can be operated in three different ways: as a PFR, a CFSTR, or as two CFSTRs in series with the detention time split equally between the two. Find the effluent concentrations for the three possible operating modes
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