Chemical Reaction Engineering

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Chemical Reaction Engineering

Kinetics, reactor design and reactor safety — the interactive lecture series

21 interactive lectures 40 live calculators and plots 28 animated machines 39 interactive exercises 547 glossary terms · 86 quiz questions RMPE410 · 4 ECTS · WS 2026/27

The lectures

Each lecture opens in the browser and works on a phone as well as a projector. Navigate with the arrow keys or by swiping.

← → previous / next slide T contents G glossary F presentation mode tap any underlined term for its definition
LECTURE 01

Introduction

What chemical reaction engineering is for, the five model reactors, and the one balance equation that generates all of their design equations.

reactor familyfirst sizingquiz
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LECTURE 02

Balance Equations

The chemical system, stoichiometric coefficients, the extent of reaction Ξ, and the general mole balance — in, out, generation, accumulation.

extent calculatorcontrol volumequiz
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LECTURE 03

Tank Reactors

The hardware behind the perfectly-mixed assumption: impellers, baffles, the Newton–Reynolds power characteristic and P/V scale-up.

stirred tankpower numberquiz
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LECTURE 04

Tube Reactors

Plug flow and the differential mole balance, multitubular industrial forms, and why a PFR always beats a CSTR for a positive-order rate.

tube bundlePFR vs CSTRquiz
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LECTURE 05

Conversion

Conversion X, the four design equations rewritten in X, and the Levenspiel plot — the rectangle and the area under the curve.

live Levenspiel plotSimpsonquiz
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LECTURE 06

Reactors in Series

Cascades, the staircase construction, N tanks approaching a PFR, and why the order of a mixed train matters.

staircasecascade calculatorquiz
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LECTURE 07

Rate Laws

Order, elementary reactions, the units of k, half-lives, non-elementary and Langmuir–Hinshelwood forms, and reversible rate laws.

rate plotterfind the orderquiz
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LECTURE 08

The Arrhenius Equation

k = A exp(−EA/RT): the energy barrier, the Arrhenius plot, the 10 K rule of thumb, and why extrapolation is dangerous.

Arrhenius plotEA from two pointsquiz
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LECTURE 09

Isothermal Reactors

Stoichiometric tables, the feed ratio Θ, the expansion factor ε, and every concentration written in terms of one variable.

live stoich tablegas expansionquiz
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LECTURE 10

Isothermal Reactors — Examples

The design algorithm end to end: SO2 oxidation, an LHHW packed bed, N2O4 dissociation and a laboratory-to-plant scale-up.

worked exampleslive sizingquiz
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LECTURE 11

Batch Reaction Times

How long the vessel must be held, and the cycle time that decides how many batches a year the plant actually makes.

cycle-time Ganttintegral methodquiz
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LECTURE 12

Damköhler Numbers

One dimensionless group that compares a laboratory reactor with a plant reactor: Da = τk, and conversion as a function of it.

X vs Dascale-upquiz
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LECTURE 13

Pressure Drop

The Ergun equation, the coupled p–X system, and why a gas-phase packed bed punishes you twice.

profile plotErgunquiz
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LECTURE 14

Active Intermediates

Radicals, the pseudo-steady-state hypothesis, Lindemann fall-off, and chain reactions from initiation to termination.

chain reactionfall-offquiz
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LECTURE 15

Enzymatic Reactions

Michaelis–Menten from PSSH, KM and vmax, the three inhibition types, and the chemostat with its washout limit.

MM + Lineweaver–Burkchemostatquiz
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LECTURE 16

Residence Time Distribution

What a real reactor actually does: tracer experiments, E(t) and F(t), tanks in series, dispersion, and conversion from an RTD.

RTD explorertracer dataquiz
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LECTURE 17

Multiple Reactions

Selectivity and yield: the concentration lever, the temperature lever, series reactions and the optimum quench time.

series plotselectivityquiz
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LECTURE 18

Catalysis

The seven steps at a catalyst pellet, Langmuir isotherms, LHHW rate laws, and deactivation by sintering, coking and poisoning.

pellet cross-sectionLHHWquiz
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LECTURE 19

Nonisothermal Design

The energy balance joins the mole balance: adiabatic temperature rise, the X–T diagram and multi-bed converters with interstage cooling.

X–T diagramΔTadquiz
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LECTURE 20

Unsteady-State Nonisothermal Design

Start-up transients, multiple steady states, and the ignition–extinction hysteresis that a heat balance predicts and a controller cannot fix.

G(T) vs R(T)start-upquiz
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LECTURE 21

Reactor Safety

Runaway and the Semenov diagram, ΔTad and time to maximum rate, the layers of protection, and the accidents that taught the discipline.

Semenov diagramlayers of protectionquiz
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Course information

At a glance

RMPE410Course number
4ECTS credits
21Lectures + project
  • Prerequisite: none. You will need a spreadsheet and a solver for ODEs and nonlinear equations.
  • The design project is the voluntary component that can lift your final grade.

Course literature

  • Fogler: Elements of Chemical Reaction Engineering, 6th ed. (2020) or 5th ed. (2016) — the required text
  • Fogler: Essentials of Chemical Reaction Engineering, 3rd ed. (2017)
  • Levenspiel: Chemical Reaction Engineering, 3rd ed., Wiley (1999)
  • Green & Southard: Perry’s Chemical Engineers’ Handbook, 9th ed.
  • Cutlip & Shacham: Problem Solving in Chemical and Biochemical Engineering, 2nd ed.

How to study with these lectures

  • Click every underlined term — the definition opens in place
  • Tap every part of every machine diagram; those descriptions are exam material
  • Move the sliders on every calculator until the trend stops surprising you
  • Take each quiz until you score full marks, then re-derive the key equation on paper

The spine of the course

1 · The balance

  • L01–L06 — the general mole balance, the five model reactors, conversion and cascades. One equation, five special cases.

2 · The kinetics

  • L07–L12 — rate laws, Arrhenius, stoichiometry, batch times and the Damköhler number that ties the laboratory to the plant.

3 · The complications

  • L13–L18 — pressure drop, reaction mechanisms, enzymes, real flow patterns, selectivity and catalysis.

4 · The energy balance

  • L19–L21 — nonisothermal design, transients and multiple steady states, and reactor safety.

◆ About this edition

Interactive edition of the Chemical Reaction Engineering (RMPE410) lecture series, rebuilt for WS 2026/27 by Prof. Dr. Purev-Ochir Togtokhbaatar — restructured, checked equation by equation and extended with worked calculations and live plots.