MaximaLabs
All examples
Simulation gallery

Ethylene oxide synthesis through to glycol

EpoxidationReactorHydrationGlycol production
See it live
Open this exact flowsheet in the workspace, already solved — tweak a spec and re-run.
Launch interactive model

The full EO/MEG chain in one flowsheet, upstream of the standalone hydration example: ethylene and oxygen react over a silver catalyst to ethylene oxide (low per-pass ethylene conversion, ~10%, is realistic — high conversion pushes the competing total-combustion side reaction, which this model represents as a second reactor consuming a fixed share of the same ethylene at ~80% EO selectivity). A cooled flash condenses EO (and reaction water) from the unreacted ethylene/oxygen/CO2 vented for combustion-side purge; the condensed EO then hydrates with fresh water to MEG exactly as in the standalone hydration example. No ethylene/O2 recycle loop (an honest simplification — real plants recycle unreacted ethylene at high ratio).

The flowsheet

The solved topology — every unit op's real duty, conversion, or split, read straight off a genuine converged solve.

Ethylene FEED
O2 FEED
MIX0
Epoxrx
Combrx
Cool0
Condense
Purge GAS
Waterfeed
MIX1
RXN
Cool1
Degas
EO VENT
feed
dist
btms
COL
Water Recycle
MEG Product

The stream table

Every stream's flow, temperature, pressure, and composition — real converged numbers, not placeholders.

See it live
Open this exact flowsheet in the workspace, already solved — tweak a spec and re-run.
Launch interactive model

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