IP Library Granted Patent US 6,908,873
Granted Patent B2
US 6,908,873 · App. 10/326,042 · Granted Jun 21, 2005

Regeneration of spent supported metal catalysts

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Quick Facts
Patent No.
US 6,908,873
App. No.
10/326,042
Granted
Jun 21, 2005
Kind
B2
Abstract

A method for regenerating spent supported metal catalysts comprising treating the spent catalyst with an organo-metallic complex forming agent having an ionization constant pK 1 of at least 2.5. The catalyst activity is restored to an activity level near to or greater than the fresh catalyst. The regeneration method is particularly useful for regenerating spent palladium catalysts on an alumina support as utilized for the hydrogenation of ethyl anthraquinone (EAQ) in the production of hydrogen peroxide.

Claims (34)

1. A method for regenerating a used supported metal catalyst, comprising:

(a) providing a used metal catalyst comprising a support and at least one catalytically active metal comprising metal particle clusters attached to the support;

(b) contacting the used supported metal catalyst with at least one organo-metallic complexing agent having an ionization constant pK 1 of at least about 2.5; and

(c) breaking down the metal particle clusters and relocating the at least one catalytically active metal as smaller metal particles on the support to yield a regenerated supported metal catalyst.

2. The method of claim 1 wherein the catalytically active metal comprises one or more noble metals selected from the group consisting of supported palladium, platinum, rhenium, gold, osmium, iridium, rhodium, ruthenium, and combinations thereof.

3. The method of claim 1 wherein the catalytically active metal comprises one or more metals selected from the group consisting of nickel, copper, iron, cobalt, zinc, silver, chromium, vanadium, titanium, molybdenum, tungsten, manganese, scandium, aluminum, gallium, indium, tin, antimony, lead, bismuth, sodium, potassium, lithium, beryllium, calcium, magnesium, lanthanum, cerium, and combinations thereof.

4. The method of claim 1 wherein said supported metal catalyst further comprises one or more non-metals or semimetals selected from the group consisting of boron, carbon, nitrogen, oxygen, fluorine, phosphorus, silicon, sulfur, chlorine, germanium, arsenic, selenium, bromine, tellurium, iodine, and combinations thereof.

5. The method of claim 1 wherein said support comprises porous and/or nonporous supports selected from the group consisting of alumina, silica, titania, kieselguhr, diatomaceous earth, bentonite, clay, zirconia, magnesia, zeolites, carbon black, activated carbon, graphite, flouridated carbon, organic polymers, metals, metal alloys, and combinations thereof.

6. The method of claim 1 wherein the organo-metallic complexing agent comprises an organic chelating agent.

7. The method of claim 6 wherein said organic chelating agent comprises one or more aliphatic or aromatic mono, di, arid/or tribasic carboxylic acids.

8. The method of claim 7 wherein said aliphatic or aromatic mono, di, and/or tribasic carboxylic acids are selected from the group consisting of glycolic acid, malonic acid, tartaric acid, citric acid, succinic acid, glutaric acid, glycine, salicylic acid, isophthalic acid, 2-aminobenzoic acid, and their salts.

9. The method of claim 6 wherein said organic chelating agent comprises one or more polymers selected from the group consisting of polyacrylates, polymethacrylates, polyvinybenzoates, polyvinylsulfate, polyvinyl sulfonates, polybiphenol carbonates, polybenizimidazoles, polyvinylpyrrolidone, and polypyridines.

10. The method of claim 6 wherein said organic chelating agent comprises one or more of aliphatic or aromatic amino compounds selected from the group consisting of ethylene diamine, propylene diamine, diethylenetriamine, triethylenetetraamine, diethylenetriamine pentaacetic acid (DTPA), N-(hydroxyethyl)-ethylenediaminetriacetic acid (HEDTA), and their salts.

11. The method of claim 6 wherein said organic chelating agent comprises phosphonate compounds including amine tri(methylanephosphonic acid) (ATMP), 1-Hydroxy-1,1-diphosphonic acid (HEDP), diethylenetriamine penta (methylphosphonic) acid, and their salts.

12. The method of claim 1 where said organo-metallic complexing agent comprises one or more of an oligomeric or polymeric chelating agent containing one or more acid groups.

13. The method of claim 1 further comprising cleaning, drying and calcining the used catalyst before contacting the used catalyst with said organo metallic complexing agent.

14. The method of claim 1 wherein (b) is carried out at a temperature in a range of 0-400° C. and a pressure in a range of 0-10 atmospheres.

15. The method of claim 1 wherein (b) is carried out for a time period in a range of 1-8 hours.

16. A method for regenerating a used catalyst having supported metal catalyst particles comprising:

a) calcining the used catalyst in air; and

b) contacting the calcined catalyst from a) with at least one organo-metallic complexing agent, whereby the used catalyst is regenerated to a catalytic activity level in a range of 90-103% compared to fresh catalyst activity.

17. The method of claim 16 further including cleaning the used catalyst by contacting it with a solvent before calcining.

18. The method of claim 17 wherein the used catalyst is cleaned at a temperature in a range of 10-100° C. and a pressure in a range of 1-20 atmospheres for a time sufficient to clean the surface of the supported catalyst particles.

19. The method of claim 16 wherein the used catalyst is calcined in air at a temperature range of 350-500° C. for a time period in a range of 2-10 hours.

20. The method of claim 16 wherein the calcinced catalyst is contacted with at least one organo-metallic complexing agent at a temperature in a range of 20-400° C. and a pressure in a range of 1-5 atmospheres for a time sufficient to regenerate the catalyst.

21. The method of claim 16 wherein the organo-metallic complexing agent has a pK 1 of at least about 2.5.

22. The method of claim 16 wherein the supported metal catalyst particles comprise one or more noble metals selected from the group consisting of palladium, platinum, rhenium, gold, osmium, iridium, rhodium, ruthenium, and combinations thereof.

23. The method of claim 16 wherein said organo-metallic complexing agent is selected from the group consisting of aliphatic and/or aromatic mono, di, and/or tribasic carboxylic acids, polyacrylates, polymethacrylates, polyvinybenzoates, polyvinylsulfate, polyvinyl sulfonates, polybiphenol carbonates, polybenizimidazoles, polyvinylpyrrolidone, polypyridines, ethylene diaminc, propylene diaminc, diethylenetriamine, triethylenetctraamine, diethylenetriamine pentaccetic acid (DTPA), N-Qiydroxyethyl)-ethylenediaminetriacctic acid (HEDTA), amino tri(methylanephosphonic acid) (ATMP), 1-Hydroxy-1,1-diphosphonic acid (HEDP), diethylenetriamine penta (methylphosphonic) acid, their salts, and combinations thereof.

24. The method of claim 16 wherein the metal catalyst particles are attached to a catalyst support selected from the group consisting of alumina, silica, titania, keiselguhr, distomaceous earth, bentonite, clay, zirconia, magnesia, zeolites, carbon black, activated carbon, graphite, fluoridated carbon, organic polymers, metals, metal alloys, and combinations thereof.

25. A method for regenerating a spent supported metal catalyst comprising:

contacting the spent supported metal catalyst with at least one organo-metallic complexing agent having an ionization constant pK 1 of at least about 2.5 under conditions sufficient to regenerate the spent supported metal catalyst,

wherein the organo-metallic complexing agent comprises an organic chelating agent, wherein said organic chelating agent comprises:

(i) one or more aliphatic or aromatic mono, di, and/or tribasic carboxylic acids selected from the group consisting of glycolic acid, malonic acid, tartaric acid, citric acid, succinic acid, glutaric acid, glycine, salicylic acid, isophthalic acid, 2-aminobenzoic acid, and their salts; and/or

(ii) one or more phosphonate compounds including amine tri(methylanephosphonic acid) (ATMP), 1-Hydroxy-1,1-diphosphonic acid (HEDP), diethylenetriamine penta (methylphosphonic) acid, and their salts.

Assignments (14)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 29, 2022
From: POROCEL INTERNATIONAL, LLC
To: EVONIK OPERATIONS GMBH
Reel/Frame 060928/0221 →
PATENT RELEASE (REEL:23699/FRAME:0452) Recorded Mar 26, 2015
From: WILMINGTON TRUST, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
To: HEADWATERS INCORPORATED, AS GRANTOR; HEADWATERS RESOURCES, INC., A UTAH CORPORATION; HEADWATERS TECHNOLOGY INNOVATION GROUP, INC., A UTAH CORPORATION; HEADWATERS HEAVY OIL, LLC, A UTAH CORPORATION; TAPCO INTERNATIONAL CORPORATION, A MICHIGAN CORPORATION
Reel/Frame 035306/0558 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 19, 2014
From: HEADWATERS TECHNOLOGY INNOVATION GROUP, INC.
To: POROCEL INTERNATIONAL, LLC
Reel/Frame 032477/0381 →
SECURITY AGREEMENT Recorded Nov 20, 2009
From: HEADWATERS INCORPORATED, A DELAWARE CORPORATION; HEADWATERS CTL, LLC, A UTAH LIMITED LIABILITY COMPANY, USA; HEADWATERS HEAVY OIL, LLC, A UTAH LIMITED LIABILITY COMPANY, USA; HEADWATERS RESOURCES, INC., A UTAH CORPORATION, USA; HEADWATERS TECHNOLOGY INNOVATION GROUP, INC., A UTAH CORPORATION, USA; TAPCO INTERNATIONAL CORPORATION, A MICHIGAN CORPORATION, USA
To: WILMINGTON TRUST FSB, AS COLLATERAL AGENT
Reel/Frame 023699/0452 →
RELEASE OF SECURITY AGREEMENT Recorded Oct 29, 2009
From: MORGAN STANLEY & CO. INCORPORATED
To: CURTIS-WRIGHT FLOW CONTROL CORPORATION; HEADWATERS CTL, LLC (SUCCESSOR TO HYDROCARBON TECHNOLOGIES, INC.); HEADWATERS TECHNOLOGY INNOVATION GROUP, INC. (SUCCESSOR TO HEADWATERS TECHNOLOGY INNOVATION LLC) AND INSTITUTE OF COAL CHEMISTRY; CROZZOLI, GUALTIERO; HEADWATERS TECHNOLOGY INNOVATION GROUP, INC. (SUCCESSOR TO HEADWATERS TECHNOLOGY INNOVATION LLC); HEADWATERS RESOURCES, INC. (SUCCESSOR TO JTM INDUSTRIES, INC.); TAPCO INTERNATIONAL CORPORATION (SUCCESSOR TO MID AMERICA BUILDING PRODUCTS); TAPCO INTERNATIONAL CORPORATION (SUCCESSOR TO TAPCO PRODUCTS COMPANY, INC.); HEADWATERS INCORPORATED; HEADWATERS RESOURCES, INC.; TAPCO INTERNATIONAL CORPORATION
Reel/Frame 023438/0778 →
RELEASE OF SECURITY AGREEMENT Recorded Oct 29, 2009
From: MORGAN STANLEY & CO. INCORPORATED
To: CURTIS-WRIGHT FLOW CONTROL CORPORATION; HEADWATERS CTL., LLC (SUCCESSOR TO HYDROCARBON TECHNOLOGIES, INC.); HEADWATERS TECHNOLOGY INNOVATION GROUP, INC. (SUCCESSOR TO HEADWATERS TECHNOLOGY INNOVATION LLC) AND INSTITUTE OF COAL CHEMISTRY; CROZZOLI, GUALTIERO; HEADWATERS TECHNOLOGY INNOVATION GROUP, INC. (SUCCESSOR TO HEADWATERS TECHNOLOGY INNOVATION LLC); HEADWATER RESOURCES, INC. (SUCCESSOR TO JTM INDUSTRIES, INC.); TAPCO INTERNATIONAL CORPORATION (SUCCESSOR TO MID AMERICA BUILDING PRODUCTS); TAPCO INTERNATIONAL CORPORATON (SUCCESSOR TO TAPCO PRODUCTS COMPANY, INC.); HEADWATERS INCORPORATED; HEADWATERS RESOURCES, INC.; TAPCO INTERNATIONAL CORPORATION
Reel/Frame 023449/0740 →
MERGER Recorded May 28, 2008
From: HEADWATERS NANOKINETIX, INC.
To: HEADWATERS TECHNOLOGY INNOVATION, LLC
Reel/Frame 021006/0271 →
MERGER Recorded Dec 19, 2006
From: HEADWATERS NANOKINETIX INC
To: HEADWATERS TECHNOLOGIES INNOVATION LLC
Reel/Frame 018645/0831 →
SECOND LIEN IP SECURITY AGREEMENT Recorded Oct 28, 2004
From: HEADWATERS INCORPORATED; ACM BLOCK & BRICK GENERAL, INC.; ACM BLOCK & BRICK PARTNER, LLC; ACM BLOCK & BRICK, LLC; ACM BLOCK & BRICK, LP; ACM FLEXCRETE, LP; ACM GEORGIA, INC.; AMERICAN CONSTRUCTION MATERIALS, INC.; BEST MASONRY & TOOL SUPPLY, INC.; CHIHUAHUA STONE LLC; COVOL ENGINEERED FUELS, LC; COVOL SERVICES CORPORATION; DON'S BUILDING SUPPLY, L.P.; EAGLE STONE & BRICK LLC; ELDORADO ACQUISITION, LLC; ELDORADO G-ACQUISITION CO.; ELDORADO SC-ACQUISITION CO.; ELDORADO STONE ACQUISITION CO., LLC; ELDORADO STONE CORPORATION; ELDORADO STONE FUNDING CO., LLC; ELDORADO STONE LLC; ELDORADO STONE OPERATIONS, LLC; GLOBAL CLIMATE RESERVE CORPORATION; HEADWATERS CLEAN COAL CORP.; HEADWATERS HEAVY OIL, INC.; HEADWATERS NANOKINETIX, INC.; HEADWATERS OLYSUB CORPORATION; HEADWATERS TECHNOLOGY INNOVATION GROUP, INC.; HTI CHEMICAL SUBSIDIARY, INC.; HYDROCARBON TECHNOLOGIES, INC.; ISG MANUFACTURED PRODUCTS, INC.; ISG PARTNER, INC.; ISG RESOURCES, INC.; ISG SERVICES CORPORATION; ISG SWIFT CRETE, INC.; L&S STONE LLC; L-B STONE LLC; LEWIS W. OSBORNE, INC.; MAGNA WALL, INC.; NORTHWEST PROPERTIES LLC; NORTHWEST STONE & BRICK CO., INC.; NORTHWEST STONE & BRICK LLC; PALESTINE CONCRETE TILE COMPANY, L.P.; STONECRAFT INDUSTRIES LLC; TEMPE STONE LLC; UNITED TERRAZZO SUPPLY CO., INC.; VFL TECHNOLOGY CORPORATION; ELDORADO FUNDING CO.; TAPCO HOLDINGS, INC.; TAPCO INTERNATIONAL CORPORATION; VANTAGE BUILDING PRODUCTS CORPORATION; MTP, INC.; ATLANTIC SHUTTER SYSTEMS, INC.; METAMORA PRODUCTS CORPORATION; METAMORA PRODUCTS CORPORATION OF ELKLAND; WAMCO CORPORATION; BUILDERS EDGE, INC.; COMACO, INC.
To: MORGAN STANLEY & CO. INCORPORATED
Reel/Frame 015908/0816 →
SECURITY AGREEMENT Recorded Oct 25, 2004
From: HEADWATERS INCORPORATED; ACM BLOCK & BRICK GENERAL, INC.; ACM BLOCK & BRICK PARTNER, LLC,; ACM BLOCK & BRICK, LLC,; ACM BLOCK & BRICK, LP,; ACM FLEXCRETE, LP,; ACM GEORGIA, INC.,; AMERICAN CONSTRUCTION MATERIALS, INC.,; BEST MASONRY & TOOL SUPPLY, INC.,; CHIHUAHUA STONE LLC,; COVOL ENGINEERED FUELS, LC,; COVOL SERVICES CORPORATION,; DON'S BUILDING SUPPLY, L.P.,; EAGLE STONE & BRICK LLC,; ELDORADO ACQUISITION, LLC,; ELDORADO G-ACQUISITION CO.,; ELDORADO SC-ACQUISITION CO.,; ELDORADO STONE ACQUISITION CO., LLC,; ELDORADO STONE CORPORATION,; ELDORADO STONE FUNDING CO., LLC,; ELDORADO STONE LLC,; ELDORADO STONE OPERATIONS LLC,; GLOBAL CLIMATE RESERVE CORPORATION,; HEADWATERS CLEAN COAL CORP.,; HEADWATERS HEAVY OIL, INC.,; HEADWATERS NANOKINETIX, INC.,; HEADWATERS OLYSUB CORPORATION,; HEADWATERS TECHNOLOGY INNOVATION GROUP, INC.,; HTI CHEMICAL SUBSIDIARY, INC.; HYDROCARBON TECHNOLOGIES, INC.,; ISG MANUFACTURED PRODUCTS, INC.,; ISG PARTNER, INC.,; ISG RESOURCES, INC.,; ISG SERVICES CORPORATION,; ISG SWIFT CRETE, INC.,; L&S STONE LLC,; L-B STONE LLC,; LEWIS W. OSBORNE, INC.,; MAGNA WALL, INC.,; NORTHWEST PROPERTIES LLC,; NORTHWEST STONE & BRICK CO., INC.,; NORTHWEST STONE & BRICK LLC,; PALESTINE CONCRETE TILE COMPANY, L.P.,; STONECRAFT INDUSTRIES LLC,; TEMPE STONE LLC,; UNITED TERRAZZO SUPPLY CO., INC.,; VFL TECHNOLOGY CORPORATION,; ELDORADO FUNDING CO.; TAPCO HOLDINGS, INC.,; TAPCO INTERNATIONAL CORPORATION,; VANTAGE BUILDING PRODUCTS CORPORATION,; MTP, INC.,; ATLANTIC SHUTTER SYSTEMS, INC.,; METAMORA PRODUCTS CORPORATION,; METAMORA PRODUCTS CORPORATION OF ELKLAND,; WAMCO CORPORATION,; BUILDERS EDGE, INC.,; COMACO, INC.,
To: MORGAN STANLEY & CO. INCORPORATED
Reel/Frame 015896/0667 →
RELEASE OF SECURITY INTEREST Recorded Sep 8, 2004
From: BANK ONE, NA
To: HYDROCARBON TECHNOLOGIES, INC.
Reel/Frame 015093/0519 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 7, 2004
From: HYDROCARBON TECHNOLGIES, INC. (NEW JERSEY); HYDROCARBON TECHNOGIES INNOVATION GROUP, INC; HYDROCARBON TECHNOLOGIES, INC. (UTAH)
To: HEADWATERS NANOKINETIX, INC.
Reel/Frame 015428/0415 →
SECURITY AGREEMENT Recorded Apr 23, 2004
From: HYDROCARBON TECHNOLOGIES, INC.
To: BANK ONE, NA
Reel/Frame 014556/0191 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 20, 2002
From: ZHOU, BING; RUETER, MICHAEL
To: HYDROCARBON TECHNOLOGIES, INC.
Reel/Frame 013635/0789 →