← Back to Patent Explorer
US3679746A Expired / Lapsed US ⏱️ 0.0 years remaining

Isomer enrichment of bicyclohexyl-4,4{40 -diamine

Assignee: EIDP Inc
•
Filing: 1969-10-27
•
Granted: 1972-07-25
•
Expires: 1989-10-27
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A mixture of the stereoisomers of bicyclohexyl-4,4''-diamine not at equilibrium is converted to a mixture of stereoisomers approaching the equilibrium ratio by heating the mixture of stereoisomers to a temperature of from 150* to 300* C. in the presence of hydrogen at a pressure of from 50 to 5,500 pounds per square inch gage and a total pressure of from 500 to 15,000 pounds per square inch gage, in the presence of from 0 to 200 percent by weight of added ammonia and from 0.001 to 10 percent by weight, calculated as metallic ruthenium, of a ruthenium catalyst supported on an inert carrier, both percentages being based on the weight of a starting material, said catalyst being alkali moderated with from 0.05 to 15 percent of a basic alkali metal compound calculated as the alkali metal. Either essentially pure trans,trans-bicyclohexyl-4,4''-diamine or an enriched mixture of cis,trans- and cis,cis-bicyclohexyl-4,4''-diamine can be recovered.

Inventors

  • 👤 Loren D Brake

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 08:17
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/38; B01J23/54; B01J23/56; B01J23/63; B01J23/58

Claims Analysis

Total Claims: 27
Claim 1
Independent Claim 25 words
The process of claim 1 wherein the starting material is a mixture of stereoisomers of bicyclohexyl-4,4''-diamine containing less than the equilibrium concentration of the trans,trans-stereoisomer.
Claim 2
Dependent Claim 27 words
dissolving the diamine product of step (1) in a solvent and cooling the solution to a temperature of from 10* to 75* C. to precipitate trans,trans-bicyclohexyl-4,4''-diamine; and
Claim 3
Dependent Claim 27 words
dissolving the diamine product of step (1) in a solvent and cooling the solution to a temperatuRe of from 10* to 75* C. to precipitate trans,trans-bicyclohexyl-4,4''-diamine; and
Claim 4
Dependent Claim 10 words
recovering the precipitate of step (2) as essentially pure trans,trans-bicyclohexyl-4,4''-diamine.
Claim 5
Dependent Claim 20 words
separating the precipitate of step (2) to obtain a solution of the stereoisomeric mixture enriched in cis,trans- and cis, cis-bicyclohexyl--4,4''-diamine.
Claim 6
Dependent Claim 14 words
The process of claim 1 wherein the amount of added ammonia is 0 percent.
Claim 7
Dependent Claim 14 words
The process of claim 2 wherein the amount of added ammonia is 0 percent.
Claim 8
Dependent Claim 20 words
The process of claim 1 wherein the liquid separated from the precipitate of step (3) is recycled to step (1).
Claim 9
Dependent Claim 34 words
The process of claim 1 wherein the catalyst carrier is selected from the group consisting of alumina, barium sulfate, kieselguhr, carbon, calcium carbonate, rare earth oxides, rare earth carbonates, and mixed rare earth oxide-carbonates.
Claim 10
Dependent Claim 21 words
The process of claim 1 wherein the catalyst carrier is selected from the group consisting of alumina, barium sulfate and kieselguhr.
Claim 11
Dependent Claim 29 words
The process of claim 1 wherein the catalyst is moderated with from 0.1 to 10 percent by weight of a basic alkali metal compound calculated as the alkali metal.
Claim 12
Dependent Claim 34 words
The process of claim 8 wherein basic alkali metal compound is selected from the group consisting of (i) the hydroxides, carbonates, bicarbonates, and alkoxides of sodium, lithium, cesium, rubidium, and potassium, and (ii) sodamide.
Claim 13
Dependent Claim 17 words
The process of claim 1 wherein the temperature in step (1) varies from 180* to 225* C.
Claim 14
Dependent Claim 17 words
The process of claim 1 wherein the essentially pure trans, trans-bicyclohexyl-4,4''-diamine contains at least 85 percent trans,trans-bicyclohexyl-4,4''-diamine.
Claim 15
Dependent Claim 16 words
The process of claim 1 wherein the essentially pure trans-trans-bicyclohexyl-4,4''-diamine contains at least 99.9 percent trans,trans-bicyclohexyl-4,4''-diamine.
Claim 16
Dependent Claim 22 words
A process for the preparation of a stereoisomeric mixture of bicyclohexyl-4,4''-diamine rich in the cis, trans- and cis,cis-stereoisomers comprising the steps of
Claim 17
Dependent Claim 27 words
The process of claim 11 wherein the starting material is a mixture of stereoisomers of bicyclohexyl-4,4''-diamine containing less than the equilibrium concentration of the cis,trans- and cis,cis-stereoisomers.
Claim 18
Dependent Claim 14 words
The process of claim 11 wherein the amount of added ammOnia is 0 percent.
Claim 19
Dependent Claim 14 words
The process of claim 12 wherein the amount of added ammonia is 0 percent.
Claim 20
Dependent Claim 17 words
The process of claim 13 wherein the precipitate separated in step (3) is recycled to step (1).
Claim 21
Dependent Claim 34 words
The process of claim 13 wherein the catalyst carrier is selected from the group consisting of alumina, barium sulfate, kieselguhr, carbon, calcium carbonate, rare earth oxides, rare earth carbonates, and mixed rare earth oxide-carbonates.
Claim 22
Dependent Claim 21 words
The process of claim 13 wherein the catalyst carrier is selected from the group consisting of alumina, barium sulfate and kieselguhr.
Claim 23
Dependent Claim 29 words
The process of claim 13 wherein the catalyst is moderated with from 0.1 to 10 percent by weight of a basic alkali metal compound calculated as the alkali metal.
Claim 24
Dependent Claim 34 words
The process of claim 20 wherein basic alkali metal compound is selected from the group consisting of (i) the hydroxides, carbonates, bicarbonates, and alkoxides of sodium, lithium, cesium, rubidium, and potassium, and (ii) sodamide.
Claim 25
Dependent Claim 17 words
The process of claim 13 wherein the temperature in step (1) varies from 180* to 225* C.
Claim 26
Dependent Claim 18 words
The process of claim 13 wherein the bicyclohexyl-4,4''-diamine product contains at least 70 percent cis,cis- and cis, trans-bicyclohexyl-4,4''-diamine.
Claim 27
Dependent Claim 18 words
The process of claim 13 wherein the bicyclohexyl-4,4''-diamine product contains at least 85 percent cis,cis- and cis, trans-bicyclohexyl-4,4''-diamine.

References Cited (Backward Citations)

US2606925A Cited
US3155724A Cited
US3347917A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-07-25 1976-01-24 1976-07-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-07-25 1980-01-24 1980-07-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-07-25 1984-01-24 1984-07-25 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag