The invention relates to a
heat pipe type SCR denitration reactor and a low-temperature
sulfur-containing
flue gas denitration method thereof. A
flue and a heat source medium channel which are horizontally arranged up and down are arranged in a reactor body, a heat
insulation layer is arranged between the
flue and the heat source medium channel, a
heat pipe array is vertically arranged in the reactor body, the middle portions of heat pipes penetrate through the heat
insulation layer, a condensation section and an
evaporation section of the
heat pipe are located in the flue and the heat source medium channel respectively, and a denitration catalyst layer of a porous structure is arranged outside the condensation section of the heat
pipe. During operation, the temperature of a heat source medium needs to be higher than the temperature of
flue gas, the requirement for the
working temperature of the catalyst is met, the catalyst in the flue is maintained in a high-activity and high-
sulfur-resistance temperature window by means of the characteristics of fast
heat transfer and good axial temperature uniformity of the heat
pipe, stable low-temperature
flue gas denitration can be achieved even if a traditional medium-temperature SCR catalyst is adopted,
high energy consumption of a conventional process for overall reheating of low-temperature
flue gas is avoided, and in-situ continuous regeneration of the catalyst can be achieved by increasing the
operation temperature of a heat source medium channel after the catalyst is inactivated at low temperature.