Skip to main content
Calcimator

Reactor Sizing Calculator

Size CSTR and PFR reactors for first-order reactions using the design equation V = FA0·X/(−rA).

About this calculator

This calculator sizes a reactor for a first-order reaction using the standard chemical-reaction-engineering design equations. For a CSTR (Continuously Stirred Tank Reactor, well-mixed so the exit concentration equals the concentration everywhere inside), the volume is V = FA0·X / (−rA), where −rA = k·CA0·(1−X) is the first-order rate evaluated at the exit concentration -- this simplifies to the textbook CSTR residence-time result τ = X / [k(1−X)]. For a PFR (Plug Flow Reactor, unmixed along its length so concentration changes continuously as fluid moves through), the same design principle integrated along the reactor's length gives V = [FA0 / (k·CA0)] × [−ln(1−X)], which simplifies to τ = (1/k) × ln[1/(1−X)] -- the standard first-order PFR result.

Target Conversion is overwhelmingly the dominant driver of both Reactor Volume and Residence Time: as conversion approaches 100%, both design equations blow up (the CSTR's (1−X) denominator and the PFR's ln[1/(1−X)] term both diverge), so pushing conversion higher costs disproportionately more reactor volume the closer you get to complete conversion. Feed Concentration has NO effect on either Reactor Volume or Residence Time for a first-order reaction -- it cancels out algebraically in both design equations, since a first-order rate law scales proportionally with concentration on both sides of the balance. Feed Volumetric Flow Rate scales Reactor Volume directly (more flow needs more volume to hold the same residence time) but has no effect on Residence Time itself, since residence time is a per-unit-of-fluid property independent of how much total flow you're processing.

Inputs

L/min
mol/L
1/min

Results

Reactor Volume

400 L

≈ 5 wheelbarrows

Residence Time

40 min

Space Time (τ)40 min
Exit Concentration0.4 mol/L
How to Use This Calculator
  1. Enter the Feed Volumetric Flow Rate in L/min and the Feed Concentration in mol/L.
  2. Enter the Target Conversion as a decimal (e.g., 0.80 = 80% conversion of the reactant).
  3. Enter the First-Order Rate Constant (k) in 1/min at the operating temperature — obtain from kinetics experiments or literature.
  4. Select the Reactor Type: CSTR (Continuously Stirred Tank Reactor, well-mixed) or PFR (Plug Flow Reactor, unmixed axially).
  5. Read the Reactor Volume in liters — a PFR always requires less volume than a CSTR for the same conversion and first-order kinetics.
  6. Review the Residence Time (τ) in minutes and Exit Concentration in mol/L to confirm the design meets purity requirements.

How the result changes with Target Conversion

Target ConversionReactor VolumeResidence Time
0.466.67 L6.67 min
0.6150 L15 min
0.999,900 L990 min

What each input means

Feed Volumetric Flow Rate
Volumetric flow rate of the feed entering the reactor.
Feed Concentration
Molar concentration of the reactant in the feed stream (CA0).
Target Conversion
Desired fractional conversion of the reactant (0 to 1).
Rate Constant (k)
First-order reaction rate constant at operating temperature.
Reactor Type
CSTR (well-mixed) or PFR (plug flow, unmixed axially).

How this is calculated

Worked example, using the default values

  1. Identify Input Parameters
    5 parameters
    Feed Volumetric Flow Rate = 10, Feed Concentration = 2, Target Conversion = 0.8, Rate Constant (k) = 0.1, Reactor Type = 1 = 5 input(s) provided
  2. Calculate Reactor Volume
    V = FA0 × X ÷ [k × CA0 × (1 − X)] (CSTR)
    FA0=20.000 mol/min, CA0=2, X=0.8, k=0.1, Type=CSTR = 400 L
  3. Calculate Residence Time
    τ = V ÷ v0
    400 ÷ 10 = 40 min
  4. Calculate Space Time
    τ_space = V ÷ v0 (constant density, equals Residence Time)
    400 ÷ 10 = 40 min
  5. Calculate Exit Concentration
    CA_exit = CA0 × (1 − X)
    2 × (1 − 0.8) = 0.4 mol/L

Engine last updated . Checked against 5 independently-derived tests — how we verify calculators. Built by Paul Gunder, a software engineer, not a licensed financial, medical, or legal professional.

Frequently Asked Questions

Why does Feed Concentration have no effect on Reactor Volume or Residence Time?

For a first-order reaction, the rate law −rA = k·CA scales directly with concentration, and the design equations for both CSTR and PFR are built from ratios of concentration terms that cancel Feed Concentration out algebraically -- doubling Feed Concentration doubles both the molar feed rate and the rate of reaction by the same factor, leaving the required volume unchanged. This is a genuine property of first-order kinetics, not a coincidence of these particular default values, and this calculator verifies it holds across the full declared input range.

Why does Reactor Volume grow so much faster as I push Target Conversion toward 100%?

Both design equations contain a term that diverges as conversion approaches 100% -- the CSTR's volume is proportional to X/(1−X), and the PFR's is proportional to ln[1/(1−X)] -- so each additional percentage point of conversion near the high end costs disproportionately more reactor volume than the same percentage-point increase near the low end. This is why real processes often target 90-99% conversion rather than chasing 100%: the last few percent gets extremely expensive in reactor size.

Why does Feed Volumetric Flow Rate change Reactor Volume but not Residence Time?

Residence Time (τ = V/v0) is a per-unit-of-fluid property -- how long a given parcel of fluid spends in the reactor -- so it depends only on the reaction kinetics (Rate Constant) and Target Conversion, not on how much total flow you're processing. Reactor Volume, on the other hand, scales directly with Feed Volumetric Flow Rate because processing more flow at the same residence time simply requires a proportionally bigger tank or pipe to hold it all.

For the same conversion and kinetics, does a CSTR or PFR need more volume?

A PFR always requires less volume than a CSTR to reach the same conversion with the same first-order kinetics, because a CSTR operates entirely at its (lower) exit concentration throughout its whole volume, while a PFR's concentration -- and therefore its reaction rate -- stays higher through most of its length before dropping off near the exit. That higher average reaction rate lets a PFR reach the same conversion in less volume; the gap between the two grows larger as Target Conversion increases.

What does the Rate Constant (k) actually represent, and where does it come from?

Rate Constant is the first-order reaction rate constant at your operating temperature -- it sets how fast the reaction proceeds independent of concentration, with units of inverse time (1/min here). It isn't something this calculator derives; you obtain it from kinetics experiments (measuring concentration decay over time at a fixed temperature) or from published literature values for your specific reaction and temperature, since rate constants for the same reaction can vary by orders of magnitude across different temperatures.

The questions that sit next to this one — chosen by subject, including calculators filed under a different category.

More in Engineering.