The utility model relates to the technical field of
chemical engineering, and discloses a C4 extraction separation
solvent regeneration energy-saving
system which comprises a light component removal
tower system and a heavy component removal
tower system, the light component removal
tower system comprises a light component removal tower, a light component removal tower
water cooler, a light component removal tower
reflux tank, a light component removal tower
reflux pump and a light component removal tower kettle delivery pump; the de-heavy tower system comprises a de-heavy tower, a de-heavy tower
water cooler, a de-heavy tower
reflux tank, a de-heavy tower reflux pump and a
vacuum pump. A
solvent from which intermediate component impurities are to be removed firstly enters a heavy component removal tower to be separated,
nitrogen formylmorpholine and heavy components are separated from a tower kettle, tower top effluents are methyl ethyl
ketone and intermediate components, methyl ethyl
ketone and the intermediate components enter a light component removal tower to be separated, methyl ethyl
ketone flows out of the light component removal tower top, and light component removal tower kettle liquid is the intermediate components, so that the intermediate components are removed; the temperatures of the light component removal tower kettle and the heavy component removal tower kettle are both 160 DEG C, and the
steam pressure is 0.8 MPa, so that the requirements can be met, and the
energy consumption is reduced.