The invention belongs to the technical field of
fluorine chemical industry, and particularly relates to a
continuous production process of heptafluoroisobutyryl
fluoride. The process is carried out in a tubular reactor, the tubular reactor is divided into a first preheating section, a second reaction section and a third reaction section, a fluorinated
molecular sieve catalyst is filled in the second reaction section and the third reaction section, each reaction section is respectively heated to a corresponding preset temperature,
carbonyl fluoride and
hexafluoropropylene which are mixed and preheated are introduced into the tubular reactor, and a fluorinated
molecular sieve catalyst is introduced into the tubular reactor. Enabling the gas to sequentially flow through each section of the tubular reactor, contacting and reacting with the fluorinated
molecular sieve catalyst in the second reaction section and the third reaction section, and condensing the gas discharged from the outlet end of the tubular reactor to obtain a heptafluoroisobutyryl
fluoride product. According to the process,
carbonyl fluoride and
hexafluoropropylene are used as gas-
phase reaction raw materials, and heptafluoroisobutyryl
fluoride is synthesized through a one-step
continuous flow rapid reaction. The reaction
route is short, the reaction conversion rate and selectivity are high, and industrial large-scale production is easy to realize.