IP Library Granted Patent US 10,421,212
Granted Patent B2
US 10,421,212 · App. 15/283,796 · Granted Sep 24, 2019

Methods for making lignocellulose containing composite products

Inventors: Adam K. Sniady (Liburn, GA); Cornel Hagiopol (Liburn, GA); Derek L. Atkinson (Lawrenceville, GA); Bobby L. Williamson (Conyers, GA); John B. Hines (Atlanta, GA)
Assignee: Georgia-Pacific Chemicals LLC
B27N3/002B27N3/02B29D7/01C08H6/00C08H8/00C08J5/18C08L97/02C09J197/005
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Quick Facts
Patent No.
US 10,421,212
App. No.
15/283,796
Granted
Sep 24, 2019
Kind
B2
Abstract

Methods for making composite products are provided. In at least one specific embodiment, the method can include combining a plurality of lignocellulose substrates and one or more free radical precursors to produce a mixture of the lignocellulose substrates and the one or more free radical precursors. The method can also include maintaining the mixture at a temperature less than 60° C. for at least 10 minutes while retaining at least 11 wt % of the one or more free radical precursors charged to the mixture. The method can then include heating the mixture comprising at least 11 wt % of the one or more free radical precursors charged to the mixture to a temperature of at least 60° C. to about 300° C. to produce a composite product. The composite product can have a density less than 1 g/cm 3 and an internal bond strength of at least 0.35 MPa.

Claims (33)

1. A method for making a composite product, comprising:

combining a plurality of lignocellulose substrates and an oxidant to produce a mixture; and

heating the mixture to a temperature of 60° C. to about 300° C. to produce a composite product having an internal bond strength of at least 0.3 MPa, as measured according to ASTM D1037-06a,

wherein the mixture comprises at least 11 wt % of the oxidant initially combined with the plurality of lignocellulose substrates until the mixture reaches the temperature of 60° C.

2. The method of claim 1 , wherein the oxidant comprises hydrogen peroxide.

3. The method of claim 1 , wherein, prior to heating the mixture to the temperature of 60° C. to about 300° C. to produce the composite product, an amount of energy generated from the mixture due to any exothermic reaction is less than 20 cal/g.

4. The method of claim 1 , wherein the composite product has an internal bond strength of about 0.35 MPa to about 1.7 MPa, as measured according to ASTM D1037-06a.

5. The method of claim 1 , further comprising combining a catalyst with the plurality of lignocellulose substrates and the oxidant to produce the mixture.

6. The method of claim 5 , wherein the catalyst comprises a metal in the form of a complex bound to a complexing agent, wherein the metal comprises iron, copper, manganese, tungsten, molybdenum, cobalt, titanium, or any mixture thereof, and wherein the complexing agent comprises cyanide, sulfate, ethylenediaminetetraacetic acid, ethylenediamine-N,N′-disuccinic acid, ethyleneglycol-bis(2-aminoethyl)-N,N,N′,N′-tetraacetic acid, diethylenetriaminepentaacetic acid, trans-1,2-diaminocyclohexane tetraacetic acid, iminodisuccinate, nitrilotriacetic acid, or any mixture thereof.

7. The method of claim 5 , wherein the oxidant comprises hydrogen peroxide and the catalyst comprises one or more iron containing catalysts.

8. The method of claim 5 , wherein the oxidant comprises hydrogen peroxide and the catalyst comprises potassium ferricyanide, an iron complex of ethylenediaminetetraacetic acid, an iron complex of ethylenediamine-N,N′-disuccinic acid, an iron complex of ethyleneglycol-bis(2-aminoethyl)-N,N,N′,N′-tetraacetic acid, an iron complex of diethylenetriamine pentaacetic acid, an iron complex of trans-1,2-diaminocyclohexanetetraacetic acid, an iron complex of nitrilotracetic acid, or any mixture thereof.

9. The method of claim 5 , wherein the mixture is maintained at a temperature of less than 60° C. for at least 10 minutes prior to heating the mixture.

10. The method of claim 5 , wherein the mixture is maintained at a temperature of less than 35° C. for at least 10 minutes prior to heating the mixture.

11. The method of claim 5 , wherein the mixture comprises at least 25 wt % of the oxidant initially combined with the plurality of lignocellulose substrates until the mixture reaches the temperature of 60° C.

12. A method for making a composite product, comprising:

combining a plurality of lignocellulose substrates, a polyphenolic compound, and an oxidant to produce a mixture; and

heating the mixture to a temperature of 60° C. to about 300° C. to produce a composite product having an internal bond strength of at least 0.3 MPa, as measured according to ASTM D1037-06a,

wherein the mixture comprises at least 11 wt % of the oxidant initially combined with the plurality of lignocellulose substrates and the polyphenolic compound until the mixture reaches the temperature of 60° C.

13. The method of claim 12 , further comprising combining a catalyst with the plurality of lignocellulose substrates, the polyphenolic compound, and the oxidant to produce the mixture.

14. The method of claim 13 , wherein the mixture comprises at least 20 wt % of the oxidant initially combined with the plurality of lignocellulose substrates, the polyphenolic compound, and the catalyst until the mixture reaches the temperature of 60° C.

15. The method of claim 14 , wherein the mixture is maintained at a temperature of less than 60° C. for at least 10 minutes prior to heating the mixture.

16. The method of claim 12 , wherein the oxidant comprises hydrogen peroxide, and wherein the polyphenolic material comprises lignin, tannins, a novolac resin, bisphenol A, modified phenol formaldehyde resin, humic acid, or any mixture thereof.

17. The method of claim 12 , wherein the composite product has an internal bond strength of about 0.35 MPa to about 1.7 MPa, as measured according to ASTM D1037-06a.

18. A method for making a composite product, comprising:

combining a plurality of lignocellulose substrates, a catalyst, and hydrogen peroxide to produce a mixture, wherein the mixture comprises about 0.01 wt % to about 5 wt % of the catalyst and about 0.1 wt % to about 200 wt % of the hydrogen peroxide, based on a dry weight of the plurality of lignocellulose substrates; and

heating the mixture to a temperature of 60° C. to about 300° C. to produce a composite product having an internal bond strength of at least 0.3 MPa to about 1.7 MPa, as measured according to ASTM D1037-06a,

wherein the mixture comprises at least 11 wt % of the hydrogen peroxide initially combined with the plurality of lignocellulose substrates and catalyst until the mixture reaches the temperature of 60° C.

19. The method of claim 18 , wherein the catalyst comprises a metal in the form of a complex bound to a complexing agent, wherein the metal comprises iron, copper, manganese, tungsten, molybdenum, cobalt, titanium, or any mixture thereof, and wherein the complexing agent comprises cyanide, sulfate, ethylenediaminetetraacetic acid, ethylenediamine-N,N′-disuccinic acid, ethyleneglycol-bis(2-aminoethyl)-N,N,N′,N′-tetraacetic acid, diethylenetriaminepentaacetic acid, trans-1,2-diaminocyclohexane tetraacetic acid, iminodisuccinate, nitrilotriacetic acid, or any mixture thereof.

20. The method of claim 18 , wherein:

the mixture is maintained at a temperature of less than 60° C. for at least 10 minutes prior to heating the mixture,

the catalyst comprises potassium ferricyanide, an iron complex of ethylenediaminetetraacetic acid, an iron complex of (S,S)-ethylenediamine-N,N′-disuccinic acid, an iron complex of diethylenetriamine pentaacetic acid, an iron complex of ethyleneglycol-bis(2-aminoethyl)-N,N,N′,N′-tetraacetic acid, an iron complex of trans-1,2-diaminocyclohexanetetraacetic acid, or any mixture thereof,

the mixture comprises about 0.05 wt % to about 2 wt % of the catalyst and about 1 wt % to about 30 wt % of the hydrogen peroxide, based on a dry weight of the plurality of lignocellulose substrates, and

wherein the mixture comprises at least 25 wt % of the hydrogen peroxide initially combined with the plurality of lignocellulose substrates and catalyst until the mixture reaches the temperature of 60° C.

Assignments (5)
ASSIGNMENT OF PATENT AND TRADEMARK SECURITY INTEREST Recorded May 12, 2025
From: MACQUARIE CAPITAL FUNDING LLC
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 071276/0379 →
CHANGE OF NAME Recorded Mar 13, 2025
From: GEORGIA-PACIFIC CHEMICALS LLC
To: BAKELITE CHEMICALS LLC
Reel/Frame 070495/0222 →
SECURITY INTEREST Recorded Jun 9, 2022
From: GEORGIA-PACIFIC CHEMICALS LLC; GEORGIA-PACIFIC CONSUMER PRODUCTS LP; ENERG2 TECHNOLOGIES, INC.; KOCH AGRONOMIC SERVICES LLC; BAKELITE UK HOLDING LTD.; SURFACE TECH LLC
To: GOLDMAN SACHS BANK USA, AS ADMINISTRATIVE AGENT
Reel/Frame 060328/0250 →
SECURITY INTEREST Recorded Jun 9, 2022
From: GEORGIA-PACIFIC CHEMICALS LLC; GEORGIA-PACIFIC CONSUMER PRODUCTS LP; ENERG2 TECHNOLOGIES, INC.; KOCH AGRONOMIC SERVICES LLC; BAKELITE UK HOLDING LTD.
To: MACQUARIE CAPITAL FUNDING LLC, AS ADMINISTRATIVE AGENT
Reel/Frame 060328/0327 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 25, 2018
From: SNIADY, ADAM K.; HAGIOPOL, CORNEL; ATKINSON, DEREK L.; WILLIAMSON, BOBBY L.; HINES, JOHN B.
To: GEORGIA-PACIFIC CHEMICALS LLC
Reel/Frame 046193/0499 →
Continuity (3)
Continuation 14040791 · Sep 30, 2013
Provisional Application 61708395 · Oct 1, 2012
Related Publication 20170021524A1 · Jan 26, 2017