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Bio-ethanol: energy-integrated distillation + MVR stillage concentration

DistillationVapor recompressionEnergy integrationBio-ethanol
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A dilute beer (10% ethanol) is concentrated toward the azeotrope in a beer column, and the water-rich stillage bottoms are concentrated in an evaporator whose vapor is recompressed by a mechanical-vapor-recompression (MVR) compressor — recovering the stillage vapor's latent heat as high-grade heating duty instead of venting it, the energy-integration route that eliminates a separate thermal oxidizer. Honesty note: the MVR train is modeled at screening fidelity (an evaporator + a real isentropic-efficiency recompression of its vapor, reporting the recompression work); the solids in real stillage are not tracked (the bottoms is modeled as the ethanol/water liquid), and this is an equipment-train energy study, not a rigorous three-phase superheated-steam dryer.

The flowsheet

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

BEER
feed
dist
btms
COL
Ethanol
Steam
feed
steam
conc
vapor
cond
EVAP
COMP
Syrup
Condensate
Recompressed Vapor

The stream table

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

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