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Guided lessons that teach process engineering the way a great tutor would — explain the idea, ask you to predict, have you build it in the real simulator, then reflect. Most are free for everyone; a few Pro lessons go deeper with AI tutoring and advanced thermodynamics. Pick your level.

Working toward a certificate? These lessons are the study material for certification modules — pass each module's assessment, then the capstone, to earn a verifiable credential.

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Your level

Secondary school

Ages ~14–18 · no prior chemistry-engineering needed

Plain-language introductions to how industry turns raw materials into products — the ideas first, the maths gently.

University

Undergraduate & graduate chemical engineering

The methods as they are taught and examined — distillation design, recycle structure, property-model judgement.

Separations 20 min

Shortcut distillation design (FUG)

Fenske–Underwood–Gilliland: estimate minimum stages, minimum reflux and a real stage count from your separation targets.

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Process structure 18 min

Recycle structure & convergence

Why real flowsheets loop back on themselves, how the solver tears recycles, and why a purge is unavoidable.

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Thermodynamics 16 min

Choosing a property method

When is ideal good enough, when do you need an equation of state, and when must you model activity coefficients?

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Separations 13 min

The single equilibrium stage: flash

Distillation is a stack of equilibrium stages — but the whole idea lives in one flash drum. Run one and watch volatility do the work.

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Reaction 14 min

Reactors: conversion, equilibrium, Gibbs

Three reactor models, and the judgement to pick one. See the Gibbs reactor predict an equilibrium with no reaction specified at all.

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Thermodynamics 18 min

Azeotropes & NRTL: when ideal models lie

Pro

Real polar mixtures break the simple models. Use the NRTL activity package to model the ethanol–water azeotrope that Ideal and PR get badly wrong.

Why Pro: This lesson uses the NRTL activity-coefficient package — a Pro-only thermodynamic method fitted to real vapor–liquid data — to model the ethanol–water azeotrope that Ideal and Peng-Robinson get badly wrong.

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Thermodynamics 16 min

AI property estimation for an off-databank molecule

Pro

Sooner or later your component isn't in any databank. Use AI to generate a usable property set — and learn to validate it before you trust a result.

Why Pro: This lesson uses Pro-only AI property estimation to generate a consistent property set for a component that isn't in the 3,400-component databank — with the validation flags that tell you how far to trust it — then simulates with it.

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Economics 16 min

From flowsheet to price tag: process economics

Pro

Size the equipment of a converged flowsheet, cost it with industry-standard correlations, and learn why big plants win — CAPEX the way plant-design courses teach it.

Why Pro: This lesson works inside the Pro-only Economics environment: it sizes real equipment from your converged simulation, prices it with Turton-class module costing on a live CEPCI basis, and grades you on hitting a capital budget.

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Corporate training

Graduate-engineer onboarding & upskilling

Fluency, design judgement and troubleshooting for new process engineers before they touch production tools.

Onboarding 20 min

Week 1 — Simulator fluency

Get hands-on fast: build a flash-with-recycle flowsheet from a blank canvas and converge it without peeking at the solution.

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Design judgement 22 min

Week 2 — Design to a spec at minimum duty

Meet a hard purity spec at the lowest reboiler duty you can — the everyday optimization of a working process engineer.

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Troubleshooting 20 min

Week 3 — Flowsheet troubleshooting

A loop that barely converges and a purge set wrong: diagnose with the convergence monitor, fix it, and explain why.

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Fundamentals 14 min

Reading a stream table & closing balances

A new engineer's first discipline: never trust a number from a model whose mass balance doesn't close. Audit a real column.

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AI-assisted engineering 18 min

AI co-pilot: diagnose a failing flowsheet

Pro

Modern engineers work with an AI assistant, not without one. Put the AI Process Assistant to work on a real recycle loop — and learn to catch it when it's wrong.

Why Pro: This lesson puts the Pro-only AI Process Assistant to work on a real loop — explaining results, localising a fault and proposing a fix — so you build the judgement to use it well (and catch it when it's confidently wrong).

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Economics 18 min

Week 4 — Will it make money? TEA judgement

Pro

Turn a converged design into a decision: OPEX, cost of manufacture, NPV and IRR — and the judgement to know which numbers drive the answer.

Why Pro: Runs the full Pro techno-economic analysis: utility-based OPEX from the energy balance, cost of manufacture, discounted-cash-flow profitability and sensitivity — the analysis a process engineer is asked for the first time a manager says 'nice flowsheet, but should we build it?'.

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Capstone 25 min

Capstone: a plant section with a design report

Pro

From 'it converged' to 'here is a defensible design'. Optimize a multi-unit section, get an AI review, and generate a PDF design report.

Why Pro: This capstone uses Pro-only features end to end — a larger multi-unit flowsheet, Case Study optimization, an AI design review and a generated PDF design report — to take you from 'I made it converge' to 'here is a defensible design document'.

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Worked examples to explore

Pre-built flowsheets to open, run and tinker with freely — no steps, no checks.

Benzene-Toluene DistillationClassic binary distillation: preheat a 50/50 benzene-toluene feed and separate it in a shortcut (FUG) column to 99% recoveries.Open Flash Separation with RecycleA pentane/octane stream is heated and flashed; the liquid is partly purged and partly recycled. Watch the tear-stream iteration converge.Open Ammonia Synthesis LoopHaber-Bosch in miniature: compress syngas, react N2 + 3H2 -> 2NH3 at 25% per-pass conversion, condense ammonia, purge inerts and recycle.Open Shortcut vs Rigorous ColumnThe same benzene-toluene feed split to an FUG shortcut column and a rigorous tray-by-tray (Wang-Henke) column with the shortcut's design — compare purities, duties and the stage profiles.Open Toluene Hydrodealkylation (PFR)The reactor section of the classic HDA process: toluene + H2 → benzene + CH4 in an adiabatic plug-flow reactor with power-law kinetics (r = k·C_T·C_H2^0.5, teaching parameters), then quench and flash.Open Ethanol-Water Column (NRTL)ProDistill a 20 mol% ethanol beer feed toward the azeotrope using NRTL activity coefficients. See why simple distillation cannot pass ~89 mol% ethanol.Open Lime Kiln (Solids)A solids line end to end: crush 10 t/h of limestone (with a quartz impurity), screen out oversize, and calcine the fines — CaCO3 → CaO + CO2 at +178 kJ/mol — in a kiln at ~900 °C.Open Water Electrolyser (Electrometallurgy)Split water into hydrogen and oxygen in an electrochemical cell driven at ~386 kA. Production follows Faraday's law exactly; the cell reports power, specific energy (kWh/kg H2) and the heating/cooling duty relative to the thermoneutral voltage.Open Zinc Leach & Electrowinning (Hydrometallurgy)A hydrometallurgy line: leach zinc calcine (ZnO) in sulfuric acid to a pregnant liquor + residue, then electrowin zinc metal from the liquor — regenerating acid and evolving oxygen. The leach duty and the EW specific energy (~3 kWh/kg Zn) fall out of formation enthalpies and Faraday's law.Open Carbothermic Iron Smelting (Pyrometallurgy)Smelt hematite ore with coke at ~1600 °C: 2 Fe2O3 + 3 C → 4 Fe + 3 CO2. Iron deports to the molten metal phase, the silica gangue to slag, and CO2 to the top gas. The duty covers the endothermic reduction, heating to tapping temperature and the latent heat of fusion of the iron.Open Ammonia Equilibrium (Gibbs Reactor)Predictive equilibrium with no reaction specified: a 1:3 N2/H2 syngas enters a Gibbs reactor at 700 K and 200 bar, which minimizes the total Gibbs energy to find the equilibrium NH3. Drop the pressure and watch the conversion collapse — Le Chatelier, computed from first principles.Open Predictive Calcination (Multi-phase Gibbs)The same limestone calcination as the lime kiln — but here NO reaction is specified. A multi-phase Gibbs reactor takes 10 t/h of calcite at 900 °C and minimizes the total Gibbs energy across the gas and solid phases, predicting for itself that CaCO3 is unstable and decomposes to CaO + CO2. A cyclone then splits the CO2 gas from the lime. Lower the temperature below ~860 °C and the reactor predicts the calcite stays intact.Open Acid Speciation & pH (Aqueous Gibbs)Pour 0.5 mol/kg sulfuric acid into water and let the Gibbs reactor predict the chemistry: it speciates the solution by free-energy minimization with electroneutrality, reporting the pH (~0.4), the ionic strength and the H+/HSO4-/SO4-- distribution. Because its ions are parameterised for it, the engine uses the more accurate Pitzer activity model rather than Davies. The acid passes through as an apparent component — the speciation is reported alongside.Open Zinc Recovery by Precipitation (Reactive Aqueous Gibbs)A reactive electrolyte equilibrium with no reaction specified: dose a zinc sulfate liquor with caustic and the Gibbs reactor predicts that ZnSO4 + 2 NaOH neutralise and precipitate Zn(OH)2 — anchored to the measured solubility product — leaving a sodium sulfate liquor. A filter then recovers the hydroxide cake. The solid leaves as a real product stream and the mass balance closes; lower the caustic dose and watch the zinc stay in solution.Open BTX Distillation — TEA BasisProThe benzene–toluene column with an economic basis attached: feed 0.45 $/kg, benzene 0.95 $/kg, toluene 0.60 $/kg. Run it, then open the Economics environment for the full CAPEX/OPEX/NPV picture.Open

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