IP Library Granted Patent US 9,499,917
Granted Patent B2
US 9,499,917 · App. 14/076,445 · Granted Nov 22, 2016

Non-Faradaic electrochemical promotion of catalytic methane reforming for methanol production

Inventor: Qinbai Fan (Chicago, IL)
Assignee: Gas Technology Institute
C25B3/02C25B1/04Y02P20/132
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Quick Facts
Patent No.
US 9,499,917
App. No.
14/076,445
Granted
Nov 22, 2016
Kind
B2
Abstract

A method of converting methane to methanol at low temperatures utilizes a reactor including an anode, a cathode, a membrane separator between the anode and cathode, a metal oxide catalyst at the anode and a hydrogen recovery catalyst at the cathode. The method can convert methane to methanol at as rate exceeding the theoretical Faradaic rate due to the contribution of an electrochemical reaction occurring in tandem with a Faradaic reaction.

Claims (15)

1. A method of converting methane to methanol, comprising the steps of:

providing a reactor including an anode, a cathode, and a membrane separator between the anode and the cathode;

feeding methane to the anode, and electrochemically converting the methane to methanol and electrons in the presence of a metal oxide catalyst at the anode;

feeding an aqueous alkaline solution to the cathode;

conducting the electrons to the cathode, thereby transforming water at the cathode to hydrogen gas and hydroxide ions;

transforming the hydroxide ions through the membrane separator to the anode, causing regeneration of the metal oxide catalyst; and

recovering the methanol from the reactor.

2. The method of claim 1 , wherein the membrane separator includes an anode side and a cathode side, further comprising the steps of providing the metal oxide catalyst on the anode side and providing a hydrogen evolution catalyst on the cathode side.

3. The method of claim 2 , wherein the hydrogen evolution catalyst comprises a metal selected from platinum, iron, ruthenium, osmium, and combinations thereof.

4. The method of claim 1 , wherein the membrane separator comprises a porous layer containing an alkaline polymer electrolyte.

5. The method of claim 1 , wherein the membrane separator comprises a porous layer containing an acidic polymer electrolyte.

6. The method of claim 1 , wherein the membrane separator comprises a porous layer containing both an alkaline polymer electrolyte and an acidic polymer electrolyte.

7. The method of claim 1 , wherein the metal oxide catalyst comprises a metal selected from the group consisting of nickel, cobalt, copper, silver, platinum gold, cerium, lead, iron, manganese, zinc, and combinations thereof.

8. The method of claim 1 , wherein the metal oxide catalyst is selected from the group consisting of nickel hydroxide, iron hydroxide, zinc hydroxide, manganese hydroxide, cobalt hydroxide, and combinations thereof.

9. The method of claim 1 , further comprising the step of feeding an aqueous acid solution to the cathode.

Assignments (2)
CONFIRMATORY LICENSE Recorded Dec 10, 2015
From: GAS TECHNOLOGY INSTITUTE
To: U.S. DEPARTMENT OF ENERGY
Reel/Frame 037256/0378 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 22, 2013
From: FAN, QINBAI
To: GAS TECHNOLOGY INSTITUTE
Reel/Frame 031784/0505 →
Continuity (3)
Continuation In Part 13670501 · Nov 7, 2012
Continuation In Part 13719267 · Dec 19, 2012
Related Publication 20150129430A1 · May 14, 2015