The utility model provides an energy-saving device for separating and purifying materials after
hydroxylation reaction of
phenol and
hydrogen peroxide, and relates to the technical field of
chemical synthesis. Materials obtained after
phenol hydrogen peroxide hydroxylation reaction are separated and purified through the extraction
tower, the extraction agent
recovery tower, the first
phenol removal
tower, the
tar removal tower, the second phenol removal tower, the
catechol removal tower, the light component removal tower and the
hydroquinone tower, the whole technological process is simple, the yield is high, and the high-purity
hydroquinone product and the high-purity
catechol product can be obtained; according to the utility model, the extraction tower is adopted to replace a
dehydration rectifying tower in the traditional process to remove phenol-containing
wastewater, so that the phenol
recovery rate is improved, and the subsequent
wastewater treatment burden is reduced; and the
tar removal tower is arranged behind the phenol removal tower I, so that the
retention time of
tar impurities in the whole process
system is shortened, and the
process safety is improved. According to the utility model, the high-temperature
waste heat at the top of the dephenolization tower I is recovered by combining
waste heat recovery with a mechanical steam recompression energy-saving technology, so that the process
energy consumption of the operation of the whole device is effectively reduced.