The invention relates to a method for continuously synthesizing 
trifluoroacetyl chloride and 
sulfuryl fluoride, which comprises the following process: continuously introducing 
sulfur trioxide and trifluorotrichloroethane (F113a) into a reaction rectifying 
tower containing a catalyst and a filler thorough the lower part in the 
tower according to a mol ratio of 1:1, wherein the temperature of the 
tower is controlled to range between 120 DEG C and 130 DEG C, and the 
reflux ratio at the top of the tower is 2.5-3; introducing tower bottoms into a 
sulfuryl chloride separating tower for rectification and separation, wherein the tower temperature is 145-150 DEG C, and the 
reflux ratio is 0.5-1.0; returning pyrosulfuryl 
chloride in the separating tower to the middle upper part of the reaction rectifying tower, heating the 
sulfuryl chloride rectified off from the top of the tower to 150 DEG C, and then introducing the rectified 
sulfuryl chloride and preheated recycled and newly-added 
hydrogen fluoride gas into a reactor containing a 
palladium / 
charcoal catalyst, wherein the 
reaction temperature is controlled to range between 150 DEG C and 160 DEG C; separating out unreacted 
hydrogen fluoride from the 
reaction product through a 
cold trap, and returning to the reactor for further use; and then absorbing and separating 
hydrogen chloride through a falling film, 
drying, compressing, and condensing to obtain the 
sulfuryl fluoride. The invention has the 
advantage of easy acquisition of raw materials, and the 
sulfuryl chloride byproduct can be directly used for the synthesis of 
sulfuryl fluoride.