System and method of dehydrogenative coupling

Patent metadata

Field	Value
Publication number	US-10500559-B2
Application number	US-201313886464-A
Country	US
Kind code	B2
Filing date	May 3, 2013
Priority date	May 5, 2012
Publication date	Dec 10, 2019
Grant date	Dec 10, 2019

Abstract

Dehydrogenative coupling can be achieved in nearly quantitative conversions and yields using a membrane reactor.

First claim

What is claimed is:

1. A system for producing a dehydrogenative coupling product comprising:
a reactor including a reactor shell and a selectively permeable tubular membrane placed inside the reactor shell so that a reaction zone is defined between an outer surface of the selectively permeable tubular membrane and an inner surface of the reactor shell, and a gas release zone is defined by an inner surface of the selectively permeable tubular membrane;
a sweep gas line connected to the gas release zone for removing hydrogen from the gas release zone, and
a catalyst selected from the group consisting of:

wherein the selectively permeable tubular membrane permits the hydrogen to pass through the membrane and substantially blocks a substrate and its dehydrogenative coupling product from passing through the membrane,
wherein the substrate comprises a C1-C16 primary alcohol,
wherein the selectively permeable tubular membrane includes a metal membrane formed on a solid support, the metal membrane including palladium and silver, and the solid support including aluminum oxide.

2. The system of claim 1 , wherein the gas release zone is configured to transport hydrogen out of the reactor.

3. The system of claim 1 , wherein the reaction zone surrounds the gas release zone.

4. The system of claim 1 , wherein the selectively permeable tubular membrane is cylindrical.

5. The system of claim 1 , wherein a thickness of the metal membrane is 5 μm.

6. The system of claim 1 , wherein the substrate and the catalyst are substantially free of solvent.

7. A system for producing a dehydrogenative coupling product comprising:
a reactor including a reactor shell and a selectively permeable tubular membrane,
wherein a reaction zone is defined between an outer surface of the selectively permeable tubular membrane and an inner surface of the reactor shell,
wherein a gas release zone, which is separated by the selectively permeable tubular membrane from the reaction zone, is defined by an inner surface of the selectively permeable tubular membrane,
wherein the selectively permeable tubular membrane permits hydrogen to pass through the membrane and substantially blocks a substrate and its dehydrogenative coupling product from passing through the membrane,
wherein the selectively permeable membrane includes a metal membrane formed on a solid support, the metal membrane including palladium and silver, and the solid support including aluminum oxide;
a sweep gas line connected to the gas release zone, defined by the selectively permeable tubular membrane, for removing hydrogen from the gas release zone; and
a catalyst selected from the group consisting of:

8. The system of claim 7 , wherein the gas release zone is configured to transport hydrogen out of the reactor.

9. The system of claim 7 , wherein the reaction zone surrounds the gas release zone.

10. The system of claim 7 , wherein the selectively permeable tubular membrane is cylindrical.

11. The system of claim 7 , wherein a thickness of the metal membrane is 5 μm.

12. The system of claim 7 , wherein the substrate and the catalyst are substantially free of solvent.

Assignees

• Univ King Abdullah Sci & Tech

Inventors

• Huang Kuo-Wei
• Lai Zhiping

Classifications

• B01J2219/00135

  Electric resistance heaters · CPC title

• B01J23/462

  Ruthenium · CPC title

• B01J19/2475

  Membrane reactors · CPC title

• C07C67/00

  Preparation of carboxylic acid esters · CPC title

• B01J31/189

  containing both nitrogen and phosphorus as complexing atoms, including e.g. phosphino moieties, in one at least bidentate or bridging ligand · CPC title