The invention discloses a desolventizing process for producing ethyl chrysantheate, which comprises the following steps: S1, stirring and desolventizing: opening a cyclizing liquid feeding valve and a
vacuum tube valve of an efficient desolventizing
tower, pumping a certain amount of cyclizing liquid into the efficient desolventizing
tower in vacuum, closing the cyclizing liquid feeding valve and the
vacuum tube valve, opening a manual emptying tube emptying valve to enable the interior of the efficient desolventizing
tower to return to normal pressure, and then adding a catalyst into the efficient desolventizing tower; opening a
gas phase feeding valve, a
reflux valve and a circulating water inlet and outlet valve of the condenser of the efficient desolventizing tower; by adopting the three-stage desolventizing
system, the removal of the 2, 5-dimethyl-2, 4-hexadiene can be divided into three stages for desolventizing, so that the 2, 5-dimethyl-2, 4-hexadiene with higher purity is separated from the cyclization liquid to the greatest extent, the recovered purity of the
solvent and the 2, 5-dimethyl-2, 4-hexadiene is higher, the
utilization rate of the
raw material is improved, the 2, 5-dimethyl-2, 4-hexadiene is promoted to be recycled, and the yield of the 2, 5-dimethyl-2, 4-hexadiene is increased. The 2, 5-dimethyl-2, 4-hexadiene is low in
impurity content, high in quality and capable of being directly recycled, and compared with conventional
desolvation, the yield of the ethyl chrysanthemumate can be greatly increased.