Process for producing 1,2,3,4-tetrachlorohexafluorobutane
View Patent ↗The present invention provides a process for producing 1,2,3,4-tetrachlorohexafluorobutane having a high purity at a low cost industrially and efficiently. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to the present invention comprises a step of allowing 1,2,3,4-tetrachlorobutane to react with a fluorine gas to prepare a reaction product containing 1,2,3,4-tetrachlorohexafluorobutane and hydrogen-containing compounds as an impurity, and a step of introducing the reaction product into single or plural distillation columns and distilling to separate the hydrogen-containing compounds from the reaction product and thereby preparing purified 1,2,3,4-tetrachlorohexafluorobutane wherein the at least one of distillation columns has a theoretical plate number of 15 or more.
1. A process for producing 1,2,3,4-tetrachlorohexafluorobutane comprising:
a step (1) of allowing 1,2,3,4-tetrachlorobutane to react with a fluorine gas to produce a reaction product comprising 1,2,3,4-tetrachlorohexafluorobutane and hydrogen-containing compounds as an impurity, and
a step (2) of introducing the reaction product into single or plural distillation columns and distilling to separate the hydrogen containing compounds from the reaction product and thereby preparing purified 1,2,3,4-tetrachlorohexafluorobutane,
wherein the distillation columns comprise a first distillation column having a theoretical plate number of 15 or more and a second distillation column having a theoretical plate number of 25 or more, and
the step (2) comprises a step (2a) of introducing the reaction product into the first distillation column and distilling and thereby separating the hydrogen-containing compounds from the reaction product to prepare a distillate mainly containing 1,2,3,4-tetrachlorohexafluorobutane from the top of the first distillation column, and a step (2b) of introducing the distillate into the second distillation column and distilling to prepare purified 1,2,3,4-tetrachlorohexafluorobutane from the bottom of the second distillation column.
2. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to claim 1 wherein at least one of the distillation columns has a theoretical plate number of 25 to 50.
3. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to claim 1 wherein at least one of the hydrogen-containing compounds is 1,2,3,4-tetrachlorotrifluorobutane, 1,2,3,4-tetrachlorotetrafluorobutane or 1,2,3,4-tetrachloropentafluorobutane.
4. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to claim 1 wherein the reaction product prepared in the step (1) has a concentration of 1,2,3,4-tetrachlorohexafluorobutane of not less than 80% by mass.
5. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to claim 1 wherein the reaction product prepared in the step (1) has a concentration of the hydrogen-containing compounds of not more than 7.0% by mass.
6. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to claim 1 wherein the 1,2,3,4-tetrachlorohexafluorobutane purified in the step (2) has a purity of not less than 99.0% by mass.
7. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to claim 2 wherein the 1,2,3,4-tetrachlorohexafluorobutane purified in the step (2) has a purity of not less than 99.95% by mass.
8. The process for producing 1,2,3,4-tetrachlorohexafluorobutane according to claim 1 wherein the 1,2,3,4-tetrachlorohexafluorobutane purified in the step (2b) has a purity of not less than 99.99% by mass.