IP Library Granted Patent US 7,879,271
Granted Patent B2
US 7,879,271 · App. 11/792,451 · Granted Feb 1, 2011

Obtaining fiber textures of carbon by carbonizing a cellulose precursor

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,879,271
App. No.
11/792,451
Granted
Feb 1, 2011
Kind
B2
Abstract

A method of obtaining fiber textures of carbon from a cellulose precursor includes the steps of: spinning cellulose filaments ( 12 ) from a viscose solution or a cellulose solution; subjecting the cellulose filaments to washing in water ( 21 ); impregnating the washed and non-dried cellulose filaments with an aqueous emulsion ( 41 ) of at least one organosilicon additive; drying the impregnated cellulose filaments; and obtaining a fiber texture made up of impregnated and dried cellulose filaments prior to carbonization.

Claims (29)

1. A method of obtaining a fiber texture of carbon from a cellulose precursor, the method including the steps of:

spinning cellulose filaments from a viscose solution or a cellulose solution;

subjecting the cellulose filaments to washing in water;

subsequently impregnating the washed and non-dried cellulose filaments with an aqueous emulsion of at least one carbonization-enhancing organosilicon additive;

drying the impregnated cellulose filaments to obtain dried cellulose filaments provided with said carbonization-enhancing organosilicon additive;

making a fiber texture made up of said impregnated and dried cellulose filaments provided with said carbonization-enhancing organosilicon additive, the making of the fiber texture including a step of forming a yarn or unidirectional sheet from a plurality of said impregnated and dried cellulose filaments; and

carbonizing the fiber texture.

2. A method according to claim 1 , wherein the aqueous emulsion includes 5% to 50% by weight of organosilicon additive(s).

3. A method according to claim 1 , wherein, after being impregnated by the aqueous emulsion and prior to drying, the filaments are squeezed so as to obtain a water content lying in the range 10% to 50% by weight of the dry filaments.

4. A method according to claim 1 , wherein the organosilicon additive content lies in the range 1.5% to 15% by weight relative to the total weight of the filaments after drying.

5. A method according to claim 1 , wherein, after drying and prior to carbonization, a yarn is formed by twisting a plurality of impregnated and dried filaments.

6. A method according to claim 1 , wherein, after drying and prior to carbonization, a unidirectional fiber sheet is formed comprising a plurality of impregnated and dried filaments disposed substantially in parallel with one another.

7. A method according to claim 5 , wherein, prior to carbonization, a unidirectional sheet is formed comprising a plurality of yarns disposed substantially parallel to one another.

8. A method according to claim 6 , wherein the carbonization includes a stage of slow pyrolysis during which the temperature is raised progressively up to a value lying in the range 360° C. to 750° C.

9. A method according to claim 8 , wherein, during the slow pyrolysis stage, tension is applied to the yarn or the unidirectional sheet so that the variation in longitudinal dimension after pyrolysis lies in the range −30% to +40%.

10. A method according to claim 5 , wherein, prior to carbonization, a bidimensional or tridimensional fiber texture is formed by weaving, knitting or braiding yarns formed from impregnated and dried filaments.

11. A method according to claim 10 , wherein the carbonization includes a stage of slow pyrolysis during which the temperature is raised progressively up to a value lying in the range 360° C. to 750° C.

12. A method according to claim 8 , wherein, after the slow pyrolysis stage, a stage of final carbonization is performed by heat treatment at high temperature lying in the range 1200° C. to 2800° C.

13. A method according to claim 12 , wherein, during the high temperature final carbonization stage, tension is applied to the fiber texture in such a manner as to obtain elongation of not more than 200% in the longitudinal direction.

14. A method according to claim 12 , wherein, subsequently to a final carbonization stage at a temperature greater than 2500° C., the fiber texture is subjected to a further heat treatment at a temperature greater than 2500° C. and for a duration of at least 15 minutes to cause development of whiskers within the carbon fibers of the yarn or unidirectional sheet.

15. A method according to claim 8 , wherein, prior to slow pyrolysis, a relaxation stage is performed in air at a temperature lower than 200° C.

16. A method according to claim 15 , characterized in that the relaxation stage is performed at a temperature lying in the range 160° C. to 190° C.

17. A method according to claim 2 , wherein:

after being impregnated by the aqueous emulsion and prior to drying, the filaments are squeezed so as to obtain a water content lying in the range 10% to 50% by weight of the dry filaments;

the organosilicon additive content lies in the range 1.5% to 15% by weight relative to the total weight of the filaments after drying;

after drying and prior to carbonization, either a yarn is formed by twisting a plurality of impregnated and dried filaments, or a unidirectional fiber sheet is formed comprising a plurality of impregnated and dried filaments disposed substantially in parallel with one another;

the carbonization includes a stage of slow pyrolysis during which the temperature is raised progressively up to a value lying in the range 360° C. to 750° C.;

during the slow pyrolysis stage, tension is applied to the yarn or the unidirectional sheet so that the variation in longitudinal dimension after pyrolysis lies in the range −30% to +40%;

after the slow pyrolysis stage, a stage of final carbonization is performed by heat treatment at high temperature lying in the range 1200° C. to 2800° C.

Assignments (5)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 2, 2018
From: SAFRAN CERAMICS
To: ARIANEGROUP SAS
Reel/Frame 047396/0416 →
CHANGE OF NAME Recorded Aug 13, 2018
From: HERAKLES S.A.
To: SAFRAN CERAMICS S.A.
Reel/Frame 046627/0055 →
CHANGE OF NAME Recorded Apr 22, 2018
From: HERAKLES
To: SAFRAN CERAMICS
Reel/Frame 046678/0455 →
MERGER Recorded Jan 29, 2014
From: SNECMA PROPULSION SOLIDE
To: HERAKLES
Reel/Frame 032135/0709 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 18, 2009
From: OLRY, PIERRE; SOUMAILLES, CHRISTOPHE; PAILLER, RENE; LOISON, SYLVIE; KONIG, ROMAN; GUETTE, ALAIN
To: SNECMA PROPULSION SOLIDE
Reel/Frame 022279/0361 →