IP Library Granted Patent US 8,778,495
Granted Patent B2
US 8,778,495 · App. 13/563,879 · Granted Jul 15, 2014

Phenol-formaldehyde novolac resin having low concentration of free phenol

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Quick Facts
Patent No.
US 8,778,495
App. No.
13/563,879
Granted
Jul 15, 2014
Kind
B2
Abstract

A phenol-formaldehyde novolac resin having a low concentration of free phenol prepared by distilling residual phenol from a molten novolac resin and replacing at least a portion of the phenol with a solvent having a volatility equal to or less than phenol. Such modified novolac resins are suitable for the production of resin coated molding sands for shell molding and sand cores, as well as for the production of resin coated proppants for use in oil and gas recovery operations.

Claims (34)

1. A coated particle, comprising:

a particle selected from the group consisting of sand, silica, ceramic, and bauxite; and

a coating comprising:

a solid phenol-formaldehyde novolac resin containing less than 0.5 wt % free phenol; and

about 1 wt % to about 8 wt % of a non-phenolic solvent consisting of a mixture of dibasic esters, wherein the solid phenol-formaldehyde novolac resin with the non-phenolic solvent has a melt viscosity of 1,260 cps at 150° C. to less than 5,000 cps at 150° C., wherein the mixture of dibasic esters comprises about 20 wt % to about 35 wt % dimethyl adipate, about 65 wt % to about 80 wt % dimethyl glutarate, and up to 3 wt % dimethyl succinate, wherein the solid phenol-formaldehyde novolac resin has a melting point of 77° C. to 93° C., and wherein the coating contains no other non-phenolic solvent.

2. The coated particle of claim 1 , wherein the particle is ceramic.

3. The coated particle of claim 1 , wherein the particle is sand.

4. The coated particle of claim 1 , wherein the solid phenol-formaldehyde novolac resin is prepared at a phenol to formaldehyde molar ratio of 1:0.6 to 1:0.8.

5. The coated particle of claim 1 , wherein the non-phenolic solvent is present in an amount between 2 wt % and 6 wt %.

6. The coated particle of claim 1 , wherein the coating further comprises a crosslinking agent, and wherein the solid phenol-formaldehyde novolac resin is cured.

7. The coated particle of claim 1 , wherein the coating further comprises a wax and a crosslinking agent.

8. The coated particle of claim 1 , wherein the coated particle is a proppant.

9. The coated particle of claim 1 , wherein the coated particle is a foundry mold aggregate.

10. The coated particle of claim 1 , wherein the solid phenol-formaldehyde novolac resin has the melt viscosity of 1,260 cps at 150° C. to less than 4,000 cps at 150° C.

11. The coated particle of claim 1 , wherein the solid phenol-formaldehyde novolac resin has the melt viscosity of 1,260 cps at 150° C. to less than 3,000 cps at 150° C.

12. A method comprising:

depositing a coating at least partially onto a particle selected from the group consisting of sand, silica, ceramic, and bauxite, wherein the coating comprises:

a solid phenol-formaldehyde novolac resin containing less than 0.5 wt % free phenol; and

about 1 wt % to about 8 wt % of a non-phenolic solvent consisting of a mixture of dibasic esters, wherein the solid phenol-formaldehyde novolac resin with the non-phenolic solvent has a melt viscosity of 1,260 cps at 150° C. to less than 5,000 cps at 150° C., wherein the mixture of dibasic esters comprises about 20 wt % to about 35 wt % dimethyl adipate, about 65 wt % to about 80 wt % dimethyl glutarate, and up to 3 wt % dimethyl succinate, wherein the solid phenol-formaldehyde novolac resin has a melting point of 77° C. to 93° C., and wherein the coating contains no other non-phenolic solvent.

13. The method of claim 12 , wherein the particle is sand and the coating further comprises a wax and hexamine.

14. The method of claim 12 , wherein prior to depositing the coating at least partially onto the particle, the method further comprises:

at least partially reacting a mixture comprising phenol and formaldehyde to provide a first phenol-formaldehyde novolac resin comprising free phenol;

removing at least a portion of the free phenol from the first phenol-formaldehyde novolac resin to provide a second phenol-formaldehyde novolac resin having a reduced free phenol content relative to the first phenol-formaldehyde novolac resin; and

adding the non-phenolic solvent to the second phenol-formaldehyde novolac resin having the reduced free phenol content to form the solid phenol-formaldehyde novolac resin.

15. The method of claim 14 , wherein the first phenol-formaldehyde novolac resin is prepared from the mixture comprising phenol and formaldehyde at a phenol to formaldehyde molar ratio of 1:0.6 to 1:0.8.

16. The method of claim 12 , wherein the solid phenol-formaldehyde novolac resin has the melt viscosity of 1,260 cps at 150° C. to less than 4,000 cps at 150° C.

17. The method of claim 12 , wherein the method further comprises introducing the coated particle to a subterranean formation.

18. A coated proppant, comprising:

a particle selected from the group consisting of silica, ceramic, and bauxite; and

a coating disposed at least partially on the particle, wherein the coating comprises:

a solid phenol-formaldehyde novolac resin containing less than 0.5 wt % free phenol; and

about 1 wt % to about 8 wt % of a non-phenolic solvent consisting of a mixture of dibasic esters, wherein the mixture of dibasic esters comprises about 20 wt % to about 35 wt % dimethyl adipate, about 65 wt % to about 80 wt % dimethyl glutarate, and up to 3 wt % dimethyl succinate, wherein the solid phenol-formaldehyde novolac resin with the non-phenolic solvent has a melt viscosity of 1,260 cps at 150° C. to less than 5,000 cps at 150° C., wherein the solid phenol-formaldehyde novolac resin has a melting point of 77° C. to 93° C., and wherein the coating contains no other non-phenolic solvent.

19. The coated proppant of claim 18 , wherein the coating further comprises a wax and hexamine.

20. The coated proppant of claim 18 , wherein the particle is ceramic.

Assignments (4)
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 →