Method for preparing diamino-dicyclohexyl methane
US-9580380-B2 · Feb 28, 2017 · US
US11964259B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11964259-B2 |
| Application number | US-202017135515-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 28, 2020 |
| Priority date | Dec 31, 2019 |
| Publication date | Apr 23, 2024 |
| Grant date | Apr 23, 2024 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives is provided. The catalyst composition includes a carrier including aluminum oxide and magnesium oxide, a rhodium-ruthenium active layer loaded on the surface of the carrier, and a solvent including an organic amine. The weight percentage of magnesium oxide in the carrier is between 12% and 30%. A method for preparing 4,4′-methylene bis(cyclohexylamine) derivatives using the catalyst composition is also provided.
Opening claim text (preview).
What is claimed is: 1. A catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives, comprising: a carrier comprising aluminum oxide and magnesium oxide, the carrier having a surface and an interior, wherein the magnesium oxide in the carrier has a weight percentage from 12% to 30%; a rhodium-ruthenium active layer loaded on the surface of the carrier; and a solvent comprising an organic amine. 2. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the magnesium oxide has a concentration which exhibits a decreasing gradient distribution from the surface to the interior of the carrier. 3. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the carrier has a specific surface area from 150 m 2 /g to 250 m 2 /g. 4. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the weight percentage of the magnesium oxide in the carrier is in a range from 14% to 25%. 5. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the interior of the carrier consists of the aluminum oxide, and the surface of the carrier consists of magnesium aluminum oxide. 6. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 5 , wherein magnesium oxide and aluminum oxide in the magnesium aluminum oxide have a weight ratio from 2:1 to 1:2. 7. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 5 , wherein the magnesium aluminum oxide in the carrier has a weight percentage from 20% to 50%. 8. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein rhodium and ruthenium in the rhodium-ruthenium active layer have a weight ratio from 40:60 to 10:90. 9. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the rhodium-ruthenium active layer and the carrier have a weight ratio from 1:24 to 1:16. 10. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the organic amine comprises aniline, cyclohexylamine, dicyclohexyl amine, o-toluidine, 2-methylaniline, 2-methylcyclohexylamine, 2,6-dimethylaniline, 2,6-dimethylcyclohexylamine, 2-ethyl-6-methyl aniline, 2-ethyl-6-methylcyclohexylamine, 4,4′-methyl ene bis(cyclohexylamine) derivatives, or a combination thereof. 11. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 10 , wherein the 4,4′-methylene bis(cyclohexylamine) derivatives are represented by formula (I): wherein R1, R2, R3 and R4, independently, comprise H, CH 3 , C 2 H 5 or C 3 H 7 . 12. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the solvent further comprises tetrahydrofuran (THF). 13. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the solvent does not comprise tetrahydrofuran, alcohols or ethers. 14. The catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 , wherein the 4,4′-methylenedianiline derivatives comprise substituted or unsubstituted 4,4′-methylenedianiline. 15. A method for preparing 4,4′-methylene bis(cyclohexylamine) derivatives, comprising: placing a catalyst composition for hydrogenating 4,4′-methylenedianiline derivatives as claimed in claim 1 in a reactor; and introducing 4,4′-methylenedianiline derivatives and hydrogen into the reactor to proceed a hydrogenation reaction to prepare 4,4′-methylene bis(cyclohexylamine) derivatives. 16. The method for preparing 4,4′-methylene bis(cyclohexylamine) derivatives as claimed in claim 15 , wherein the reactor comprises a continuous reactor. 17. The method for preparing 4,4′-methylene bis(cyclohexylamine) derivatives as claimed in claim 15 , wherein the reactor comprises a trickle-bed reactor, a bubble-cap column reactor, or a loop reactor. 18. The method for preparing 4,4′-methylene bis(cyclohexylamine) derivatives as claimed in claim 15 , wherein the hydrogenation reaction has a hydrogen pressure from 60 bar to 80 bar. 19. The method for preparing 4,4′-methylene bis(cyclohexylamine) derivatives as claimed in claim 15 , wherein the hydrogenation reaction has a temperature from 100° C. to 160° C. 20. The method for preparing 4,4′-methylene bis(cyclohexylamine) derivatives as claimed in claim 15 , wherein the 4,4′-methylenedianiline derivatives are represented by formula (II): wherein R1, R2, R3 and R4, independently, comprise H, CH 3 , C 2 H 5 or C 3 H 7 .
Rhodium · CPC title
the fluid flow within the bed being predominantly vertical · CPC title
Magnesium; Oxides or hydroxides thereof · CPC title
100-500 m2/g · CPC title
Impregnation and coating simultaneously · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.