IP Library Granted Patent US 10,808,068
Granted Patent B2
US 10,808,068 · App. 15/881,425 · Granted Oct 20, 2020

Manufacture of novolacs and resoles using lignin

Inventors: Anthony Maiorana (Louisville, KY); Srirama N. Maddipatla Venkata (San Diego, CA); Stephen W. Arbuckle (Louisville, KY); Ganapathy Viswanathan (Louisville, KY)
Assignee: HEXION INC.
C08G8/24C08G8/08C08H6/00C08H8/00
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Quick Facts
Patent No.
US 10,808,068
App. No.
15/881,425
Granted
Oct 20, 2020
Kind
B2
Abstract

Processes for manufacturing novolacs and resoles from lignin are disclosed. A phenol-aldehyde-lignin dispersion is formed which can then be used to make either a novolac or a resole, depending upon the catalysts used.

Claims (18)

1. A process comprising:

a) heating a mixture of a first phenol, lignin, and a first catalyst comprising an acidic compound or a basic compound to a temperature in the range of from 100° C. to 200° C. to form a dispersion;

b) cooling the dispersion to a temperature in the range of 60° C. to 99° C.;

c) adding an aldehyde to the dispersion;

d) condensing the dispersion to form a phenol-aldehyde-lignin dispersion having from 1 to 10 weight percent of free aldehyde;

e) cooling the phenol-aldehyde-lignin dispersion;

f) adding a second phenol to the phenol-aldehyde-lignin dispersion;

g) condensing the phenol-aldehyde-lignin dispersion under reflux conditions in the presence of a second catalyst comprising an acidic compound to form a novolac having from 0.01 to 1 weight percent free aldehyde; and

h) vacuum distilling the novolac to produce a vacuum distilled novolac having from 0.01 to 10 weight percent free phenol.

2. The process of claim 1 , wherein in step c), the aldehyde is added to the dispersion in an amount in the range of from 0.9 to 4.5 moles of aldehyde per mole of phenol.

3. The process of claim 1 , wherein in step f), the second phenol is added to the phenol-aldehyde-lignin dispersion to provide a molar ratio of aldehyde to phenol of 0.1 to 0.9 moles of aldehyde per mole of phenol.

4. The process of claim 1 , wherein the lignin is selected from the group consisting of lignosulfonates, lignosulfonate salts, kraft lignins, pyrolytic lignins, steam explosion lignins, organosolv lignins, soda-ash lignins, dilute acid lignins, biorefinery lignins, and combinations thereof.

5. The process of claim 1 , wherein the lignin is present in the mixture of step a) in an amount in the range of from 1 weight percent to 60 weight percent.

6. The process of claim 1 , wherein the first phenol and second phenol are the same or different and are selected from the group consisting of phenol, o-methylphenol, p-methylphenol, m-methylphenol, para-tert-butyl phenol, p-octylphenol, p-phenylphenol, p-cumylphenol, p-isopropylphenol, p-nonylphenol, 2,3-dimethylphenol, 2,4-dimethylphenol, 2,5-dimethylphenol, 2,6-dimethylphenol, 3,4-dimethylphenol, 3,5-dimethylphenol, o-ethylphenol, m-ethylphenol, p-ethylphenol, bisphenol-A, resorcinol, catechol, alpha-naphthol, beta-naphtol, cardanol, and combinations thereof.

7. The process of claim 1 , wherein the aldehyde is selected from the group consisting of formaldehyde, paraformaldehyde, trioxane, acetaldehyde, polyoxymethylene, propionaldehyde, isobutyraldehyde, glyoxal, gluteraldeyhde, benzaldehyde, acrolein, crotonaldehyde, furfural, 5-hydromethylfural, and combinations thereof.

8. The process of claim 1 wherein the first catalyst is selected from the group consisting of sodium metal, sodium hydroxide, potassium metal, potassium hydroxide, lithium hydroxide, ammonium hydroxide, magnesium hydroxide, calcium hydroxide, barium hydroxide, sodium carbonate, sodium bicarbonate, potassium carbonate, potassium bicarbonate, potassium phosphate, sodium phosphate, lithium phosphate, ethanol amine, diethanol amine, triethanol amine, triethyl amine, tributyl amine, hexamine, melamine, hexamethylene diamine, guanidine, benzoguanamine, hydrochloric acid, sulfuric acid, phosphoric acid, nitric acid, oxalic acid, formic acid, acetic acid, trifluoroacetic acid, methane sulfonic acid, and p-toluenesulfonic acid; and wherein the second catalyst is selected from the group consisting of hydrochloric acid, sulfuric acid, phosphoric acid, nitric acid, oxalic acid, formic acid, acetic acid, trifluoroacetic acid, benzoic acid, methane sulfonic acid, and p-toluenesulfonic acid .

9. The process of claim 1 , further comprising i) adding a crosslinker to the vacuum distilled novolac.

10. The process of claim 9 , wherein the crosslinker is selected from the group consisting of hexamine, epoxy resins, resoles, polyisocyanates, paraformaldehyde, polybenzoxazines, cyanate esters, and combinations thereof.

Assignments (18)
SECURITY INTEREST Recorded May 12, 2025
From: BAKELITE CHEMICALS LLC; BAKELITE UK HOLDING LTD.; BAKELITE GMBH; BAKELITE SYNTHETICS UK
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 071090/0740 →
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 →
SECURITY INTEREST Recorded Jan 23, 2025
From: BAKELITE CHEMICALS LLC; BAKELITE UK HOLDING LTD.; BAKELITE GMBH; BAKELITE SYNTHETICS UK LIMITED
To: GOLDMAN SACHS BANK USA
Reel/Frame 069981/0468 →
RELEASE OF SECURITY INTEREST Recorded Jun 15, 2022
From: GOLDMAN SACHS SPECIALTY LENDING GROUP, L.P.
To: HEXION VAD LLC
Reel/Frame 060209/0558 →
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 →
CHANGE OF NAME Recorded May 3, 2022
From: HEXION VAD LLC
To: BAKELITE LLC
Reel/Frame 059926/0973 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 3, 2022
From: BAKELITE LLC
To: BAKELITE UK HOLDING LTD.
Reel/Frame 060377/0699 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 30, 2021
From: HEXION INC.
To: HEXION VAD LLC
Reel/Frame 057323/0086 →
RELEASE OF SECURITY INTEREST Recorded May 12, 2021
From: JPMORGAN CHASE BANK, N.A.
To: HEXION INC.
Reel/Frame 056219/0582 →
RELEASE OF SECURITY INTEREST Recorded May 12, 2021
From: JPMORGAN CHASE BANK, N.A.
To: HEXION INC.
Reel/Frame 056219/0677 →
SECURITY INTEREST Recorded May 5, 2021
From: HEXION VAD LLC
To: GOLDMAN SACHS SPECIALTY LENDING GROUP, L.P., AS COLLATERAL AGENT
Reel/Frame 056145/0957 →
PATENT SECURITY INTEREST (ABL) Recorded Jul 12, 2019
From: HEXION INC.
To: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT
Reel/Frame 049740/0770 →
PATENT SECURITY INTEREST (TERM LOAN) Recorded Jul 12, 2019
From: HEXION INC.
To: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT
Reel/Frame 049741/0425 →
SECURITY INTEREST Recorded Feb 1, 2019
From: HEXION INC.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 048216/0628 →
SECURITY INTEREST Recorded Feb 1, 2019
From: HEXION INC.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 048216/0683 →
SECURITY INTEREST Recorded May 22, 2018
From: HEXION INC.
To: WILMINGTON TRUST COMPANY, AS COLLATERAL AGENT
Reel/Frame 045872/0920 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 2, 2018
From: MAIORANA, ANTHONY; MADDIPATLA VENKATA, SRIRAMA N.; ARBUCKLE, STEPHEN; VISWANATHAN, GANAPATHY
To: HEXION INC.
Reel/Frame 045413/0608 →
Continuity (1)
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