How to simulate superheated-steam drying loop with mvr heat recovery

A wet cake is dried in a superheated-steam dryer (steam as the drying medium instead of hot air), and the evaporated moisture — pure steam — is recovered by mechanical vapor recompression (MVR) plus a trim superheater into high-grade superheated steam that reheats the recirculating drying medium. Superheated-steam drying is the energy-efficient route for biofuel and food solids (distillers' grains, beet pulp, lignite): because the drying atmosphere is steam, the evaporated water leaves as *more steam* whose latent heat is recompressed and reused, instead of being lost in a humid exhaust. Honesty note (same posture as bioethanol-mvr-stillage): the dryer is FlowSim's screening solid-in / vapor-out convective model (computes its own latent+sensible duty; the dried-solid identity is a generic surrogate, here 'ethanol' crystals as in the solids train), and the steam recirculation is modeled OPEN — the recompressed+superheated steam is reported as the recovered drying medium rather than piped back into the bed as a closed material recycle (the dryer op has no steam inlet to close the loop into). The MVR recompression + trim superheat of the evaporated steam — the defining SSD efficiency win — is modeled with the real compressor and heater ops.