INGENIA

CHE-01

CSTR design equation

τ = (C0 − C)/(−r) = X C0 /(−r) for constant density.

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ReactorsLevenspielFogler

Governing equation

τ=C0−CkC=Xk(1−X)\tau=\dfrac{C_0-C}{kC}=\dfrac{X}{k(1-X)}

X∈[0.05,0.95]X \in \left[0.05, 0.95\right]

where

k
Rate constant (1/s)
X
Conversion (—)
\tau
Space time (s)

The figure, part by part

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①

Governing law — red

τ=C0−CkC=Xk(1−X)\tau=\dfrac{C_0-C}{kC}=\dfrac{X}{k(1-X)}

X∈[0.05,0.95]X \in \left[0.05, 0.95\right]

X=0.05X = 0.05τ=1.053\tau = 1.053

②

Domain of the variable — blue

Xmin⁡=0.05,Xmax⁡=0.95X_{\min} = 0.05,\quad X_{\max} = 0.95

X∈[0.05,0.95]X \in \left[0.05, 0.95\right]

X=0.05X = 0.05X=0.05X = 0.05

③

Response curve — green

τ=C0−CkC=Xk(1−X)\tau=\dfrac{C_0-C}{kC}=\dfrac{X}{k(1-X)}

X∈[0.05,0.95]X \in \left[0.05, 0.95\right]

X=0.05X = 0.05τ=1.053\tau = 1.053

④

Rate of change — amber

dτdX\frac{\mathrm{d}\tau}{\mathrm{d}X}

X∈[0.05,0.95]X \in \left[0.05, 0.95\right]

X=0.056X = 0.056τ′=22.43\tau^{\prime} = 22.43

Lecture brief

Historical brief

From CSTR/PFR mole balances and Arrhenius rates to McCabe–Thiele stages and NTU exchangers, chemical engineering is conservation plus equilibrium. The lab is that design arithmetic. This sheet (CHE-01 — CSTR design equation) is the form associated with Levenspiel · Fogler. Working symbols: kk, XX →\rightarrow τ\tau. A steady mole balance around a perfectly mixed tank is V = FA0 X /(−r); dividing by volumetric flow gives the space time.

Purpose

Purpose: compute τ\tau from kk, XX in Chemical engineering via τ=C0−CkC=Xk(1−X)\tau=\dfrac{C_0-C}{kC}=\dfrac{X}{k(1-X)} τ = (C0 − C)/(−r) = X C0 /(−r) for constant density. Use it when a real chemical engineering question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given k=0.050 1/sk = 0.050\,\mathrm{1/s}, X=0.800 —X = 0.800\,\mathrm{—}, the governing relation τ=C0−CkC=Xk(1−X)\tau=\dfrac{C_0-C}{kC}=\dfrac{X}{k(1-X)} yields τ=80.000 s\tau = 80.000\,\mathrm{s}. Irreversible first-order, isothermal, constant density. Move a slider: the numbers are this situation, not a canned story.

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Inputs

Outputs

  • Space time \tau80.000 s
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Narration of this film

Irreversible first-order, isothermal, constant density.

A steady mole balance around a perfectly mixed tank is V = FA0 X /(−r); dividing by volumetric flow gives the space time.

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Watch on YouTube