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Lewis acid halide catalysts for preparation of polyamines

Assignee: Huntsman Corp
•
Filing: 1981-04-28
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Granted: 1983-08-16
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Expires: 2001-04-28
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Abstract

Abstract A process for selectively preparing predominantly non-cyclic polyalkylene polyamine compounds is disclosed wherein an alkylene polyamine compound is contacted with an alkanolamine compound in the presence of a catalytically effective amount of a Lewis acid halide substance at a temperature of from 200° to 350° C. under a pressure sufficient to maintain the reaction mixture essentially in liquid phase. The polyalkylene polyamine thus formed is recovered from the reaction mixture.

Inventors

  • 👤 Michael E. Ford
  • 👤 Thomas A. Johnson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 21:29
CPC Classifications
C; C07; C07C; C07C213/00; C07C213/08

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 160 words
A process for preparing a noncyclic polyalkylene polyamine which comprises: contacting an alkyleneamine compound having two primary amino groups of the general formula: ##STR4## wherein R is hydrogen or a lower alkyl (C 1 -C 4 ) radical, x is a number from 2 to about 6, and y is a number from 1 to about 4 with an alkanolamine compound having a primary or secondary hydroxyl group of the general formula: ##STR5## wherein R' is hydrogen or a lower alkyl (C 1 -C 4 ) radical, x' is a number from 2 to about 6; and y' is a number from 0 to about 3; the contacting being performed in the presence of an effective amount of a Lewis acid halide substance which is tin (IV) chloride, zinc chloride or zinc fluoride at a temperature sufficient to effect reaction between the alkyleneamine and the alkanolamine compounds under a pressure sufficient to maintain the reaction mixture essentially in liquid phase.
Claim 2
Dependent Claim 160 words
A process for preparing a noncyclic polyalkylene polyamine which comprises: contacting an alkyleneamine compound having two primary amino groups of the general formula: ##STR4## wherein R is hydrogen or a lower alkyl (C 1 -C 4 ) radical, x is a number from 2 to about 6, and y is a number from 1 to about 4 with an alkanolamine compound having a primary or secondary hydroxyl group of the general formula: ##STR5## wherein R' is hydrogen or a lower alkyl (C 1 -C 4 ) radical, x' is a number from 2 to about 6; and y' is a number from 0 to about 3; the contacting being performed in the presence of an effective amount of a Lewis acid halide substance which is tin (IV) chloride, zinc chloride or zinc fluoride at a temperature sufficient to effect reaction between the alkyleneamine and the alkanolamine compounds under a pressure sufficient to maintain the reaction mixture essentially in liquid phase.
Claim 3
Dependent Claim 36 words
The process of claim 1 wherein the level of the Lewis acid halide substance is from about 0.01 to 10.0 mole percent based upon the total amount of alkylenediamine and alkanolamine present in the reaction mixture.
Claim 4
Dependent Claim 36 words
The process of claim 2 wherein the level of the Lewis acid halide substance is from about 0.05 to 5.0 mole percent based upon the total amount of alkylenediamine and alkanolamine present in the reaction mixture.
Claim 5
Dependent Claim 16 words
The process of claim 2 wherein the temperature is from about 200° C. to 350° C.
Claim 6
Dependent Claim 18 words
The process of claim 4 wherein the molar ratio of alkylenediamine to alkanolamine is from 1:10 to 10:1.
Claim 7
Dependent Claim 18 words
The process of claim 5 wherein the molar ratio of alkylenediamine to alkanolamine is from 1:5 to 5:1.
Claim 8
Dependent Claim 15 words
The process of claim 5 wherein the alkylenediamine is ethylenediamine and the alkanolamine is ethanolamine.
Claim 9
Dependent Claim 15 words
The process of claim 7 wherein the temperature is from about 250° to 300° C.
Claim 10
Dependent Claim 168 words
A process for preparing a linear polyalkylene polyamine which comprises: contacting an alkyleneamine compound having two primary amino groups of the general formula: ##STR6## wherein R is hydrogen or methyl, x is a number from about 2 to 6, and y is a number from about 1 to 4 with an alkanolamine compound having a primary or secondary hydroxyl group of the general formula: ##STR7## wherein R' is hydrogen or methyl, x' is a number from about 2 to 6, and y' is a number from about 0 to 3, and the molar ratio of alkylenediamine to alkanolamine is at least 1:1; the contact being performed in the presence of about 0.01 to 10.0 mole percent, based on the total amount of alkylenediamine and alkanolamine present in the reaction mixture, of a Lewis acid halide substance which is tin (IV) chloride, zinc fluoride or zinc chloride at a temperature from about 200° to 350° C. under a pressure sufficient to maintain the reaction mixture essentially in liquid phase.
Claim 11
Dependent Claim 168 words
A process for preparing a linear polyalkylene polyamine which comprises: contacting an alkyleneamine compound having two primary amino groups of the general formula: ##STR6## wherein R is hydrogen or methyl, x is a number from about 2 to 6, and y is a number from about 1 to 4 with an alkanolamine compound having a primary or secondary hydroxyl group of the general formula: ##STR7## wherein R' is hydrogen or methyl, x' is a number from about 2 to 6, and y' is a number from about 0 to 3, and the molar ratio of alkylenediamine to alkanolamine is at least 1:1; the contact being performed in the presence of about 0.01 to 10.0 mole percent, based on the total amount of alkylenediamine and alkanolamine present in the reaction mixture, of a Lewis acid halide substance which is tin (IV) chloride, zinc fluoride or zinc chloride at a temperature from about 200° to 350° C. under a pressure sufficient to maintain the reaction mixture essentially in liquid phase.
Claim 12
Dependent Claim 20 words
The invention of claim 9 wherein the catalyst is tin (IV) chloride and the alkylenediamine:alkanolamine molar ratio is about 2:1.

References Cited (Backward Citations)

US2000410A Cited
US2085785A Cited
FR1542359A Cited
US3708539A Cited
US3714259A Cited
US3751474A Cited
US3755447A Cited
US4036881A Cited
US4044053A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-08-15 1987-02-14 1987-08-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-08-15 1991-02-14 1991-08-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-08-15 1995-02-14 1995-08-16 $7700.00 Window Closed / Lapsed

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