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Process for preparing secondary aminoether alcohols

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1983-12-23
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Granted: 1984-12-11
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Expires: 2003-12-23
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Abstract

Abstract The present invention relates to a process for selectively preparing severely sterically hindered secondary aminoether alcohols by reacting a primary amino compound with a polyalkenyl ether glycol in the presence of a hydrogenation catalyst at elevated temperatures and pressures. The severely sterically hindered secondary aminoether alcohols are useful in acid gas scrubbing processes, particularly in the selective removal of H 2 S from gaseous streams containing CO 2 and H 2 S.

Inventors

  • 👤 Eugene L. Stogryn
  • 👤 W. S. Winston Ho
  • 👤 Angelo A. Montagna
  • 👤 Guido Sartori

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 17:06
CPC Classifications
C; C07; C07C; C07C213/00; C07C213/02

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 221 words
A process for selectively producing a severely sterically hindered secondary aminoether alcohol comprising reacting: (a) a primary amino compound having the general formula R.sub.1 --NH.sub.2 where R 1 is selected from the group consisting of secondary or tertiary alkyl radicals having 3 to 8 carbon atoms and cycloalkyl radicals having 3 to 8 carbon atoms, with (b) a polyalkenyl ether glycol having the general formula: ##STR3## where R 2 , R 3 , R 4 and R 5 are each independently selected from the group consisting of hydrogen, C 1 to C 4 alkyl radicals, and C 3 -C 8 cycloalkyl radicals, with the proviso that if the carbon atom of R 1 directly attached to the nitrogen atom is secondary, at least one of R 2 and R 3 directly bonded to the carbon which is bonded to the hydroxyl group is an alkyl or cycloalkyl radical, x and y are each positive integers independently ranging from 2 to 4, and z is a positive integer ranging from 1 to 4, said process being carried out in the presence of a catalytically effective amont of a Group VIII metal containing supported hydrogenation catalyst at elevated temperatures and pressures, and wherein the mole ratio of amino compound to polyalkenyl ether glycol is less than 2:1 when z is greater than 1.
Claim 2
Dependent Claim 221 words
A process for selectively producing a severely sterically hindered secondary aminoether alcohol comprising reacting: (a) a primary amino compound having the general formula R.sub.1 --NH.sub.2 where R 1 is selected from the group consisting of secondary or tertiary alkyl radicals having 3 to 8 carbon atoms and cycloalkyl radicals having 3 to 8 carbon atoms, with (b) a polyalkenyl ether glycol having the general formula: ##STR3## where R 2 , R 3 , R 4 and R 5 are each independently selected from the group consisting of hydrogen, C 1 to C 4 alkyl radicals, and C 3 -C 8 cycloalkyl radicals, with the proviso that if the carbon atom of R 1 directly attached to the nitrogen atom is secondary, at least one of R 2 and R 3 directly bonded to the carbon which is bonded to the hydroxyl group is an alkyl or cycloalkyl radical, x and y are each positive integers independently ranging from 2 to 4, and z is a positive integer ranging from 1 to 4, said process being carried out in the presence of a catalytically effective amont of a Group VIII metal containing supported hydrogenation catalyst at elevated temperatures and pressures, and wherein the mole ratio of amino compound to polyalkenyl ether glycol is less than 2:1 when z is greater than 1.
Claim 3
Dependent Claim 29 words
The process of claim 1 wherein R 1 is an alkyl radical having 4 to 6 carbon atoms, R 4 and R 5 are hydrogen, and x is 2.
Claim 4
Dependent Claim 22 words
The process of claim 2 wherein R 1 is tertiary butyl, R 2 and R 3 are hydrogen and y is 2.
Claim 5
Dependent Claim 9 words
The process of claim 3 wherein z is 1.
Claim 6
Dependent Claim 34 words
The process of claim 1 wherein the reaction is carried out at a temperature ranging from about 160° to about 425° C. and at a pressure ranging from about 50 to about 3000 psig.
Claim 7
Dependent Claim 34 words
The process of claim 5 wherein the reaction is carried out at a temperature ranging from about 180° to about 400° C. and at a pressure ranging from about 100 to about 1000 psig.
Claim 8
Dependent Claim 35 words
The process of claim 6 wherein the reaction is carried out at a temperature ranging from about 190° to about 350° C. and at a pressure ranging from about 150 psig to about 750 psig.
Claim 9
Dependent Claim 36 words
The process of claim 4 wherein the reaction is carried out at a temperature ranging from about 190° C. to about 350° C. and at a pressure ranging from about 150 psig to about 750 psig.
Claim 10
Dependent Claim 30 words
The process of claim 1 wherein the hydrogenation catalyt is a nickel, a cobalt, a nickel-cobalt-copper, or a platinum catalyst all of which are supported on alumina, silica or alumina-silica.
Claim 11
Dependent Claim 30 words
The process of claim 8 wherein the hydrogenation catalyst is a nickel, a cobalt, a nickel-cobalt-copper, or a platinum catalyst all of which are supported on alumina, silica, or alumina-silica.

References Cited (Backward Citations)

US2355337A Cited
US2928877A Cited
US3070552A Cited
US3708539A Cited
US3660319A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-12-11 1988-06-11 1988-12-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-12-11 1992-06-11 1992-12-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-12-11 1996-06-11 1996-12-11 $7700.00 Window Closed / Lapsed

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