The invention relates to a heating method of ethyl
benzene of an ethyl
benzene dehydrogenation reaction material, which mainly solves the problems of frequent accidents of the combined
heat exchanger, difficult long-period and stable running, large pressure drop in the pipeline of a
reactive system and inadequate heat
recovery of a reactor charging / discharging three-level combined
heat exchanger in the traditional
styrene device due to the unreasonable flow for heating the ethyl
benzene by utilizing the discharging of the high temperature reactor. The invention adopts the technical proposals that a
liquid phase ethyl benzene material and ingredient
water vapor are firstly vaporized to a
gas phase with a temperature of between 90 and 110 DEG C through an independently arranged
evaporator, and then enter the third level shell pass of the reactor charging / discharging combined
heat exchanger to be preheated to a temperature of between 200 and 250 DEG C and then enter the first level shell pass of the reactor charging / discharging combined heat exchanger for being super-heated to a temperature of between 450 and 550 DEG C by the discharging of the high temperature reactor, and the second level shell pass of the reactor charging / discharging combined heat exchanger is used for generating
saturated water vapor with a pressure of between 400KPaA and 1000KPaA; and the reactor charging / discharging three-level combined heat exchanger adopts the horizontal or vertical straight-line type arrangement mode, a linear type pipeline
expansion joint is disposed between an exit of a
dehydrogenation reactor and a material inlet of the first level in the reactor charging super-heater, namely the three-level combined heat exchanger to maintain the
shortest distance for allowing installation between the
dehydrogenation reactor and the charging super-heater, thereby reducing the tube shell pass
thermal expansion difference of the first level heat exchanger.