Thermal design decides how much surface area a duty needs and how that area is arranged. We work from measured feed properties — boiling point rise, viscosity at concentration, fouling tendency — rather than assuming a clean fluid.
Key features
- Falling film, forced circulation and rising film calculations for evaporator bodies.
- Shell and tube, plate and spiral exchanger selection with fouling margin stated openly.
- Boiling point elevation and vapour load carried right through the effect train.

