The utility model discloses an energy-saving
system for
ethanol rectification. The energy-saving
system comprises a rectifying
tower, a first-stage feed preheater, a second-stage feed preheater, a third-stage feed preheater, a
tower top condenser, a
heat pump compressor, a condensation
reboiler and a
reflux tank, the first-stage, second-stage and third-stage feed preheaters are sequentially connected with the rectifying
tower; a tower top
gas phase outlet of the rectifying tower is respectively communicated with a hot side inlet of the tower top condenser and an inlet of the
heat pump compressor, an outlet of the
heat pump compressor is communicated with a hot side inlet of the condensation
reboiler, and a hot side outlet of the condensation
reboiler is communicated with a heat source inlet of the three-stage feeding preheater; a tower kettle liquid extraction port of the rectifying tower is respectively communicated with a
cold side inlet of the condensation reboiler and a heat source inlet of the secondary feeding preheater; a tower kettle liquid
backflow port of the rectifying tower is communicated with a
cold side outlet of the condensation reboiler; a first inlet of the
reflux tank is communicated with a hot side outlet of the tower top condenser, and a
liquid phase outlet of the
reflux tank is respectively communicated with a tower top reflux inlet of the rectifying tower and a heat source inlet of the primary feeding preheater. The device can reduce the consumption of tower top cooling circulating water and tower kettle steam in the rectification process, and is economical and energy-saving.