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How to simulate kinetic cstr

A continuous stirred-tank reactor with an Arrhenius first-order rate — outlet conversion comes from the kinetics, not a specified value.

Featured in:Fine Chemicals
FEED
CSTR
OUT
  1. 1
    Open the ready-made model

    Open the "Kinetic CSTR" model in the MaximaLabs workspace — no install, no license. It loads live on the canvas, ready to edit and run.

  2. 2
    Confirm the thermodynamics

    This process is modeled with the NRTL property package over ethanol, water — already selected, so the phase equilibrium and enthalpy are physically consistent from the first run.

  3. 3
    Review the flowsheet

    The flowsheet chains CSTR. Every block is a real, solvable unit op you can reconfigure on the canvas.

  4. 4
    Run the simulation

    Click Run. The deterministic solver converges the material and energy balances (recycles included) and fills the live stream table — the AI never invents a number.

  5. 5
    Read the results and iterate

    Inspect the converged streams, tweak a spec, and re-run — or ask the AI copilot to explain a result or diagnose a failed solve in plain English.

What you'll build
Thermodynamics
NRTL
Components
ethanol, water
Unit operations
CSTR
Open this model in the workspace

Opens live on the canvas — free, no install.

Explore the model & flowsheet

Frequently asked questions

What does the Kinetic CSTR model simulate?
A continuous stirred-tank reactor with an Arrhenius first-order rate — outlet conversion comes from the kinetics, not a specified value.
Which thermodynamic method does it use?
The NRTL property package, over ethanol, water — already selected. You can switch the method on the canvas before running.
Which unit operations are in the flowsheet?
It chains CSTR. Every block is a real, solvable unit operation you can reconfigure, add to, or remove.
Do I need to install software or buy a license?
No. Kinetic CSTR runs entirely in your browser on MaximaLabs — free, no install, no license. Open the model to load it live and run the deterministic solver.

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The same monomer feed, split 50/50 into two trains at equal total reactor volume: a 3-stage CSTR cascade (each stage blending its own new polymer with the MWD already carried by the stream from the stage before it) versus a single tubular (PFR) reactor. Both converge to a real, different Mn/Mw/PDI — the PFR reaches higher conversion at the same total volume, but its cumulative polydispersity is measurably broader than the cascade's, because chain length drifts continuously with conversion along the tube while each CSTR stage makes its own local production under one fixed monomer concentration. See the 'Polymerization Reactors' docs page for the full reasoning.

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An 8-stage column concentrating ethanol overhead toward the azeotrope (the headline demo).

Stop fighting legacy software. Build your first flowsheet in 60 seconds.