# Tanks in Series Model

Tanks-inTanks-in-series model

Another model that is frequently used to simulate the behavior of actual reactor networks is a cascade of ideal CSTRs operating in series. series

Tanks-inTanks-in-series model

14

The actual reactor is replaced by n identical stirred tank reactors whose total volume is the same as that of the actual reactor. 1 2

Tanks-inTanks-in-series model

Model definition:

Tanks-inTanks-in-series model

Material balance – tank N:

t t⋅E = t

N −1

NN t e − tN t ; t = N t i ; σ 2 = (N − 1)! N

2 1 t e −t t i ; t i = ; σ 2 = N t i ( N − 1)! N

2

t ti ⋅ E = ti

θi =

t = dimensionl ess time based on mean residence time per tank, t i ti t θ = = dimensionl ess time based on mean residence time in all N tanks, t t θ i = 1; θ = 1; θ i = Nθ 3

N −1

Eθ = t ⋅ E = N Eθ i = t i ⋅ E =

( N θ )N −1 e − Nθ ; σ 2 = θ ( N − 1)!

θ iN −1

e −θ i ; σ θ2i = N

1 N

(N − 1)!

4

1

Tanks-inTanks-in-series model

Chemical conversion Tanks-inTanks-in-series model

1st order reaction in one tank:

CA 1 = C A0 1 + k t

1st order reaction in N tanks-in-series:

N=

t2

σ

2

CA 1 = C A0 k t N 1 + N

5

Number of tanks-in-series N → ∞, plug flow

6

Class example

The concentration reading in the following table represents a continuous response to a pulse input. How many tanks in series is the reactor equivalent to? Time t (min) 0 5 10 15 20 25 30 35 Tracer output concentration C(t) (g/L) 0 3 5 5 4 2 1 0 7

From previous class example:

N=

t2

σ2

= 4.737 ≈ 5

8

2

Please join StudyMode to read the full document