Conjoint production of C-methyl triethylene diamine and allyl piperazine

Claim 1

A method for the conjoint manufacture of C-methyl-triethylenediamine and N-allyl piperazine which comprises bringing an aqueous solution of N-2-hydroxy-n-propyl piperazine containing about 5 to about 30 wt. % of said N-2-hydroxy-n-propyl piperazine into contact with a cyclization catalyst at a temperature of about 250°-400° C. for a period of time sufficient to conjointly convert at least a portion of said N-2-hydroxy-n-propyl piperazine to C-methyl-triethylenediamine and N-allyl piperazine; said catalyst composition consisting essentially of titania having from about 0.5 to about 7 wt. % of phosphorus thermally chemically bonded to the surface thereof in the form of phosphate bonds.

Claim 2

A method for the conjoint manufacture of C-methyl-triethylenediamine and N-allyl piperazine which comprises bringing an aqueous solution of N-2-hydroxy-n-propyl piperazine containing about 5 to about 30 wt. % of said N-2-hydroxy-n-propyl piperazine into contact with a cyclization catalyst at a temperature of about 250°-400° C. for a period of time sufficient to conjointly convert at least a portion of said N-2-hydroxy-n-propyl piperazine to C-methyl-triethylenediamine and N-allyl piperazine; said catalyst composition consisting essentially of titania having from about 0.5 to about 7 wt. % of phosphorus thermally chemically bonded to the surface thereof in the form of phosphate bonds.

Claim 3

A method for the conjoint manufacture of C-methyl-triethylenediamine and N-allyl piperazine which comprises forming an aqueous solution of N-2-hydroxy-n-propyl piperazine containing about 5 to about 30 wt. % of said N-2-hydroxy-n-propyl piperazine, continuously bringing said aqueous solution into contact with a pelleted cyclization catalyst at a temperature of about 250° to about 400° C. at a liquid hourly space velocity of about 0.2 to about 10 sufficient to convert said N-2-hydroxy-n-propyl piperazine into a reaction product predominantly containing C-methyl-triethylenediamine and N-allyl piperazine, continuously recovering an aqueous solution of said reaction product and continuously distilling said reaction product to obtain C-methyl-triethylenediamine and allyl piperazine, said catalyst composition consisting essentially of titania having from about 0.5 to about 7 wt. % of phosphorus thermally chemically bonded to the surface thereof in the form of phosphate bonds.

Claim 4

A method for the conjoint manufacture of C-methyl-triethylenediamine and N-allyl piperazine which comprises forming an aqueous solution of N-2-hydroxy-n-propyl piperazine containing about 5 to about 30 wt. % of said N-2-hydroxy-n-propyl piperazine, continuously bringing said aqueous solution into contact with a pelleted cyclization catalyst at a temperature of about 250° to about 400° C. at a liquid hourly space velocity of about 0.2 to about 10 sufficient to convert said N-2-hydroxy-n-propyl piperazine into a reaction product predominantly containing C-methyl-triethylenediamine and N-allyl piperazine, continuously recovering an aqueous solution of said reaction product and continuously distilling said reaction product to obtain C-methyl-triethylenediamine and allyl piperazine, said catalyst composition consisting essentially of titania having from about 0.5 to about 7 wt. % of phosphorus thermally chemically bonded to the surface thereof in the form of phosphate bonds.