IP Library › Granted Patent US 11,484,838
Granted Patent B2
US 11,484,838 · App. 16/941,963 · Granted Nov 1, 2022

Black liquor concentration by a membrane comprising graphene oxide on porous polymer

Inventors: Fereshteh Rashidi (Atlanta, GA); Sankar Nair (Atlanta, GA); Nikita Kevlich (Atlanta, GA); Meisha Shofner (Atlanta, GA); Scott Sinquefield (Atlanta, GA); Zhongzhen Wang (Atlanta, GA)
Assignee: Georgia Tech Research Corporation
B01D61/026B01D61/025B01D61/027B01D63/06B01D63/10B01D69/02B01D71/024D21C11/00D21C11/0042B01D69/10B01D71/68B01D2325/04B01D2325/22
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Quick Facts
Patent No.
US 11,484,838
App. No.
16/941,963
Granted
Nov 1, 2022
Kind
B2
Abstract

The disclosed technology includes a membrane-based device configured to concentrate black liquor, which results from papermaking. Certain embodiments may comprise a nanofiltration membrane configured to remove lignin from black liquor, and the nanofiltration membrane may include a first macroporous polymer substrate and a first graphene oxide membrane covering the first macroporous polymer substrate. Some embodiments may comprise a reverse osmosis membrane, which may include a second macroporous polymer substrate and a second graphene oxide membrane covering the second macroporous polymer substrate.

Claims (64)

1. A method for processing black liquor comprising:

removing from 90%-99% of lignin present in black liquor via filtering through a filtering membrane comprising:

a substrate; and

stacked non-crosslinked graphene oxide sheets forming a non-crosslinked graphene oxide membrane layer covering the substrate;

wherein the black liquor has pre- and post-filtering properties including:

a pre-filtering total solids concentration of 10 wt %, a temperature of between about 70° C. and about 95° C., and a pH of about 13; and

a post-filtering temperature of between about 70° C. and about 95° C. and a pH of about 13; and

wherein the graphene oxide membrane layer shields the substrate from exposure to the black liquor; and

wherein permeability of the graphene oxide membrane layer as measured by water permeation flux as a function of transmembrane pressure does not decrease after flowing the black liquor through the filtering membrane.

2. The method of claim 1 , wherein the lignin removed from the black liquor is between 95% and 99% of the lignin present in the pre-filtered black liquor.

3. The method of claim 1 , wherein the substrate has a thermal stability limit greater than the temperature of the black liquor and comprises a microporous polymer substrate comprising a polymer with aryl groups.

4. The method of claim 1 , wherein the substrate has a thermal stability limit greater than the temperature of the black liquor and comprises a macroporous polymer substrate comprising at least one of poly(sulfone) and poly(ethersulfone).

5. The method of claim 1 , wherein the graphene oxide membrane layer has a thickness of less than about 300 nm.

6. The method of claim 1 , wherein the substrate has a thermal stability limit greater than the temperature of the black liquor and comprises a microporous polymer substrate comprising a flat polymer sheet having a surface area greater than or equal to about 700 cm 2 .

7. The method of claim 1 , wherein the substrate has a thermal stability limit greater than the temperature of the black liquor and comprises a macroporous polymer substrate comprising flat polymer sheets,

wherein each polymer sheet has a surface area greater than or equal to about 700 cm 2 ,

wherein the filtering membrane comprises membrane sheets, each comprising a polymer sheet and the graphene oxide membrane layer, and

wherein the membrane sheets are rolled around a core tube to form a spiral wound membrane module.

8. The method of claim 1 , wherein the substrate has a thermal stability limit greater than the temperature of the black liquor and comprises a microporous polymer substrate comprising a hollow polymer tube having a surface area greater than or equal to about 100 cm 2 .

9. The method of claim 1 , wherein the substrate has a thermal stability limit greater than the temperature of the black liquor and comprises a macroporous polymer substrate comprising hollow polymer tubes,

wherein each polymer tube has a surface area greater than or equal to about 100 cm 2 ,

wherein the filtering membrane comprises membrane tubes, each comprising a hollow polymer tube and the graphene oxide membrane layer, and

wherein the membrane tubes are combined to form a tubular membrane module.

10. The method of claim 1 , wherein interlayer d-spacings of the stacked graphene oxide layers are in the range of about 3 angstroms to about 10 angstroms.

11. The method of claim 1 , wherein the filtering membrane has a molecular weight cutoff in the range of about 300 Daltons to about 1000 Daltons.

12. A method of processing black liquor comprising:

filtering a stream of black liquor through a filtering membrane comprising:

a polymer substrate; and

stacked non-crosslinked graphene oxide sheets forming a non-crosslinked graphene oxide membrane layer covering the substrate;

wherein the black liquor has pre- and post-filtering properties including:

a pre-filtering total solids concentration of 10 wt %, a temperature of between about 70° C. and about 95° C., and a pH of about 13; and

a post-filtering temperature of between about 70° C. and about 95° C. and a pH of about 13;

wherein the black liquor comprises lignin;

wherein the filtering removes at least 90% of the lignin from the black liquor;

wherein the graphene oxide membrane layer shields the substrate from exposure to the black liquor;

wherein the filtering membrane is configured to have a permeate flux in a range from about 10 kg/h·m 2 to about 30 kg/h·m 2 ; and

wherein permeability of the graphene oxide membrane layer as measured by water permeation flux as a function of transmembrane pressure does not decrease after performing for at least four days filtering the lignin from the black liquor.

13. The method of claim 12 , wherein the filtering membrane remains thermally and mechanically stable for at least 30 days filtering the lignin from the black liquor.

14. The method of claim 12 , wherein the lignin removed from the black liquor is between 95% and 99% of the lignin present in the pre-filtered black liquor.

15. The method of claim 12 , wherein the substrate is a sheet of microporous polymer substrate comprising a polymer with aryl groups having a surface area greater than or equal to about 700 cm 2 ; and

wherein the graphene oxide membrane layer has a thickness of less than about 300 nm.

16. The method of claim 12 , wherein the substrate is a sheet of macroporous polymer substrate comprising at least one of poly(sulfone) and poly(ethersulfone) having a surface area greater than or equal to about 700 cm 2 ; and

wherein the graphene oxide membrane layer has a thickness of less than about 300 nm.

17. The method of claim 12 , wherein the substrate is a macroporous polymer substrate comprising flat polymer sheets;

wherein each polymer sheet has a surface area greater than or equal to about 700 cm 2 ;

wherein the filtering membrane comprises membrane sheets, each comprising a polymer sheet and the graphene oxide membrane layer; and

wherein the membrane sheets are rolled around a core tube to form a spiral wound membrane module.

18. The method of claim 12 , wherein the substrate is a microporous polymer substrate comprising a hollow polymer tube or fiber having a surface area greater than or equal to about 100 cm 2 .

19. The method of claim 12 , wherein the substrate is a macroporous polymer substrate comprising hollow polymer tubes;

wherein each polymer tube has a surface area greater than or equal to about 100 cm 2 ;

wherein the filtering membrane comprises membrane sheets, each comprising a hollow polymer tube and the graphene oxide membrane layer; and

wherein the polymer tubes are combined to form a tubular membrane module.

20. The method of claim 12 , wherein interlayer d-spacings of the stacked graphene oxide layers are in the range of about 3 angstroms to about 10 angstroms; and

wherein the filtering membrane has a molecular weight cutoff in the range of about 300 Daltons to about 1000 Daltons.

21. The method of claim 1 , wherein the graphene oxide membrane layer remains thermally and mechanically stable under a surface flow velocity of the black liquor from about 0.22 to about 0.31 meters/second.

22. A method of processing black liquor comprising:

filtering a stream of black liquor comprising solids including lignin through a filtering membrane comprising a non-crosslinked graphene oxide membrane layer covering a substrate; and

removing at least 90% of the lignin from the black liquor;

wherein the black liquor has pre- and post-filtering properties including:

a pre-filtering total solids concentration of 10 wt %, a temperature of between about 70° C. and about 95° C., and a pH of about 13; and

a post-filtering temperature of between about 70° C. and about 95° C. and a pH of about 13:

wherein permeability of the graphene oxide membrane layer as measured by water permeation flux as a function of transmembrane pressure does not decrease after performing for at least four days filtering the lignin from the black liquor.

23. The method of claim 22 , wherein the filtering membrane remains thermally and mechanically stable for at least 30 days filtering the lignin from the black liquor.

24. The method of claim 22 , wherein the filtering removes at least 95% of the lignin when under from about 25 bar to about 30 bar of transmembrane pressure.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 24, 2020
From: NAIR, SANKAR; KEVLICH, NIKITA; RASHIDI, FERESHTEH; SHOFNER, MEISHA; SINQUEFIELD, SCOTT; WANG, ZHONGZHEN
To: GEORGIA TECH RESEARCH CORPORATION
Reel/Frame 053871/0185 →
Continuity (3)
Continuation 15702536 · Sep 12, 2017
Provisional Application 62393226 · Sep 12, 2016
Related Publication 20200368688A1 · Nov 26, 2020
Cited By (2)
US 12,357,950 US 12,397,268