CHE-01

CSTR design equation

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

Reading speed

ReactorsLevenspielFogler

Governing equation

\tau=\dfrac{C_0-C}{kC}=\dfrac{X}{k(1-X)}

where

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

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: $k$ , $X$ $\rightarrow$ $\tau$ . 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

\tau

from

k

X

in Chemical engineering via

\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\,\mathrm{1/s}

X = 0.800\,\mathrm{—}

, the governing relation

\tau=\dfrac{C_0-C}{kC}=\dfrac{X}{k(1-X)}

yields

\tau = 80.000\,\mathrm{s}

. Irreversible first-order, isothermal, constant density. Move a slider: the numbers are this situation, not a canned story.

Calculator

Inputs

Rate constant k0.05 1/sConversion X0.8 —

Outputs

Space time \tau80.000 s

Reading speed

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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.

Reading speed

Watch on YouTube