IP Library › Granted Patent US 11,590,473
Granted Patent B2
US 11,590,473 · App. 17/453,150 · Granted Feb 28, 2023

Metal supported powder catalyst matrix and processes for multiphase chemical reactions

Inventors: Gary P. Harp (Newark, DE); Jeffrey A. Knopf, Jr. (Newark, DE); William J. Napier, III (Thorndale, PA)
B01J19/1893B01J10/007B01J19/0066B01J19/1868B01J31/06B01J35/065C07C209/36B01J2231/641B01J2531/002
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Quick Facts
Patent No.
US 11,590,473
App. No.
17/453,150
Granted
Feb 28, 2023
Kind
B2
Abstract

A catalytic membrane composite that includes porous supported catalyst particles durably enmeshed in a porous fibrillated polymer membrane is provided. The porous fibrillated polymer membrane may be manipulated to take the form of a tube, disc, or diced tape and used in multiphase reaction systems. The supported catalyst particles are composed of at least one finely divided metal catalyst dispersed on a porous support substrate. High catalytic activity is gained by the effective fine dispersion of the finely divided metal catalyst such that the metal catalyst covers the support substrate and/or is interspersed in the pores of the support substrate. In some embodiments, the catalytic membrane composite may be introduced to a stirred tank autoclave reactor system, a continuous flow reactor system, or a Parr Shaker reaction system and used to effect the catalytic reaction.

Claims (13)

1. A continuous flow reaction system for multiphase reactions having at least three phases, said reaction system comprising:

a catalytic article comprising a porous fibrillated polymer membrane that includes supported catalyst particles durably enmeshed within the porous fibrillated polymer membrane;

a liquid phase comprising at least one liquid phase reactant;

a gas phase comprising at least one gas phase reactant; and

a reaction vessel configured for continuous flow of the liquid phase reactant and the gas phase reactant across and through the catalytic article,

wherein the catalytic article is in the form of a tube or a plurality of tubes bundled in a tubular array.

2. The reaction system of claim 1 , wherein the reaction system is configured for hydrogenation.

3. The reaction system of claim 1 , wherein the porous fibrillated polymer membrane is insoluble to reactants and products in the multiphase chemical reaction.

4. The reaction system of claim 1 , wherein the porous fibrillated polymer membrane comprises polytetrafluorethylene (PTFE), poly(ethylene-co-tetrafluoroethylene) (ETFE), ultra high molecular weight polyethylene (UHMWPE), polyparaxylylene (PPX), polylactic acid and any combination or blend thereof.

5. The reaction system of claim 1 , wherein the porous fibrillated polymer membrane comprises polytetrafluoroethylene (PTFE), expanded polytetrafluoroethylene (ePTFE), modified PTFE, or a PTFE copolymer.

6. The reaction system of claim 1 , wherein the porous fibrillated polymer membrane comprises expanded polytetrafluoroethylene (ePTFE).

7. The reaction system of claim 1 , wherein the porous fibrillated polymer membrane has a porosity from about 30% to about 95%.

8. The reaction system of claim 1 , wherein the reaction system is a continuous loop reactor.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 5, 2024
From: HARP, GARY P.; KNOPF, JEFFREY A., JR.; NAPIER, WILLIAM J., III
To: W. L. GORE & ASSOCIATES, INC.
Reel/Frame 067629/0706 →
Continuity (2)
Division 17043882
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