Precipitated and calcined composition based on zirconium oxide and cerium oxide
US-2015375203-A1 · Dec 31, 2015 · US
US9545617B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9545617-B2 |
| Application number | US-201514963255-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 9, 2015 |
| Priority date | Dec 9, 2014 |
| Publication date | Jan 17, 2017 |
| Grant date | Jan 17, 2017 |
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A catalyst is provided. The catalyst includes a carrier and a metal Pd. The carrier is represented by a formula: M x Al (1−x) O (3−x)/2 , where M is an alkaline earth metal, and x is between 0.09 and 0.24. The metal Pd is loaded on the carrier. A method for manufacturing the catalyst and a method for manufacturing a hydrogenated bisphenol A or derivatives thereof using the catalyst are also provided.
Opening claim text (preview).
The invention claimed is: 1. A method for manufacturing a hydrogenated bisphenol A or derivatives thereof, comprising: placing a catalyst into a reactor, wherein the catalyst comprises: a carrier, represented by a formula: M x Al (1−x) O (3−x)/2 , wherein M is an alkaline earth metal, and x is between 0.09 and 0.24; and a metal Pd, loaded on the carrier; introducing a solution containing bisphenol A or derivatives thereof into the reactor, and introducing hydrogen into the reactor, wherein the solution containing bisphenol A or derivatives thereof comprises bisphenol A or derivatives thereof and a solvent, wherein the solvent comprises a monohydric alcohol; and heating the solution containing bisphenol A or derivatives thereof in order to form a hydrogenated bisphenol A or derivatives thereof, wherein a reaction pressure is less than or equal to 70 bar, wherein the derivatives of bisphenol A comprise 2. The method for manufacturing the hydrogenated bisphenol A or derivatives thereof according to claim 1 , wherein the alkaline earth metal comprises Mg or Ca. 3. The method for manufacturing the hydrogenated bisphenol A or derivatives thereof according to claim 1 , wherein the metal Pd is between 0.5 wt % and 3 wt % based on the carrier. 4. The method for manufacturing the hydrogenated bisphenol A or derivatives thereof according to claim 1 , wherein the carrier is in amorphous phase. 5. The method for manufacturing the hydrogenated bisphenol A or derivatives thereof according to claim 1 , wherein the reaction pressure is less than or equal to 30 bar. 6. The method for manufacturing the hydrogenated bisphenol A or derivatives thereof according to claim 1 , wherein the reactor comprises a fixed bed or a trickle bed. 7. The method for manufacturing the hydrogenated bisphenol A or derivatives thereof according to claim 1 , wherein the step of heating the solution containing bisphenol A or derivatives thereof is performed at a temperature at 100° C. to 200° C.
Preparation by separation, e.g. by filtration, decantation, screening · CPC title
in a non-condensed rings substituted with hydroxy groups · CPC title
Chemistry & Metallurgy · mapped topic
Operations & Transport · mapped topic
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
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