Synthesis of C-alkyl-triethylenediamines

Claim 2

A liquid phase process for the synthesis of C-alkyl triethylenediamines comprising the steps of: initially heating a piperazine feedstock selected from a group consisting of a C-lower alkyl or C-poly lower alkyl substituted piperazine containing at least one N-(2-hydroxy ethyl) group; an unsubstituted, or C-lower alkyl substituted, or C-poly lower alkyl substituted piperazine having at least one N-(2-hydroxyalkyl) group wherein the hydroxyalkyl contains at least three carbon atoms, and mixtures thereof to elevated temperatures of about 220° C to 300° C in the presence of a catalytic amount of a pentavalent acidic phosphorus compound having at least one P--O--R group wherein R is hydrogen or a univalent organic radical and, recovering said C-alkyl triethylenediamine product.

Claim 3

The process of claim 1 wherein said catalytic amount is from about 0.1 to about 20 mol percent based upon said piperazine feedstock.

Claim 4

The process of claim 1 wherein said heating is carried out in the presence of an inert high boiling solvent having a boiling point in excess of about 250° C.

Claim 5

The process of claim 1 wherein said catalyst is selected from phosphoric acid, phosphenic acid, phosphinic acid, the corresponding organo substituted acids, the corresponding acid esters, the corresponding organo substituted acid esters, and the corresponding anhydrides.

Claim 6

A liquid phase process for the synthesis of C-alkyl triethylenediamines comprising the steps of: initially heating a piperazine feedstock of the formula ##STR3## wherein each R is, independently, a hydrogen or a monovalent hydrocarbon alkyl radical of from 1 to about 6 carbon atoms and each R' is, independently, a hydrogen or a monovalent hydrocarbon alkyl radical of from 1 to about 4 carbon atoms providing at least one of R and R' is other than hydrogen, to elevated temperatures of about 220° C to 300° C in the presence of a catalytic amount of a pentavalent acidic phosphorus compound of the formula ##STR4## wherein R" is hydrogen or a monovalent organic radical having the character of either an aliphatic or aromatic hydrocarbon; x is from 0 to 2; y is 1 or 2 and z is from 1 to 3 and the sum of x+y+z is such that P is pentavalent; and, recovering said C-alkyl triethylenediamine product.

Claim 7

A liquid phase process for the synthesis of C-alkyl triethylenediamines comprising the steps of: initially heating a piperazine feedstock of the formula ##STR3## wherein each R is, independently, a hydrogen or a monovalent hydrocarbon alkyl radical of from 1 to about 6 carbon atoms and each R' is, independently, a hydrogen or a monovalent hydrocarbon alkyl radical of from 1 to about 4 carbon atoms providing at least one of R and R' is other than hydrogen, to elevated temperatures of about 220° C to 300° C in the presence of a catalytic amount of a pentavalent acidic phosphorus compound of the formula ##STR4## wherein R" is hydrogen or a monovalent organic radical having the character of either an aliphatic or aromatic hydrocarbon; x is from 0 to 2; y is 1 or 2 and z is from 1 to 3 and the sum of x+y+z is such that P is pentavalent; and, recovering said C-alkyl triethylenediamine product.

Claim 8

The process of claim 5 wherein said catalytic amount is from about 0.1 to about 20 mol percent based upon said piperazine feedstock.

Claim 9

The process of claim 5 wherein said heating is carried out in the presence of an inert high boiling solvent having a boiling point in excess of about 250° C.

Claim 10

The process of claim 5 wherein each R is, independently, hydrogen or a lower alkyl radical of from 1 to about 4 carbon atoms.

Claim 11

The process of claim 5 wherein each R and R' are, independently, hydrogen or a methyl radical.

Claim 12

The process of claim 5 wherein each R is, independently, hydrogen and at least one of R' is a lower alkyl of from 1 to about 4 carbon atoms.

Claim 13

The process of claim 5 wherein each R' is, independently, hydrogen and at least one R is a lower alkyl of from 1 to about 4 carbon atoms.

Claim 14

The process of claim 5 wherein at least two non-adjacent R s are lower alkyl radicals of from 1 to about 4 carbon atoms and the hydroxy is attached to a primary carbon.

Claim 15

The process of claim 5 wherein said catalyst is selected from phosphoric acid; phosphinic acids and derivatives of the formula R" 2 P(O)OR" ; phosphonic acids and derivatives of the formula R"P(O)(OR" ) 2 wherein each R" is, independently, hydrogen, a lower alkyl monovalent hydrocarbon or a mono cyclic aromatic monovalent hydrocarbon radical.

Claim 16

The process of claim 5 wherein said catalyst is selected from phosphoric acid; phosphinic acid, phosphonic acid; phenylphosphinic acid; ethylphosphonic acid; phenylphosphinic acid; methylphosphinic acid; methylphenyl phosphonate; dimethylphenyl phosphonate; methylphenyl phosphinate; and propylmethyl phosphonate.