US3671192A - Method of stabilizing acrylic polymer fibers prior to graphitization - Google Patents

Method of stabilizing acrylic polymer fibers prior to graphitization Download PDF

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US3671192A
US3671192A US732514A US3671192DA US3671192A US 3671192 A US3671192 A US 3671192A US 732514 A US732514 A US 732514A US 3671192D A US3671192D A US 3671192DA US 3671192 A US3671192 A US 3671192A
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fibers
yarn
graphitization
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acrylonitrile
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Herbert M Ezekiel
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/32Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond
    • D06M11/34Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond with oxygen, ozone or ozonides
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F9/00Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
    • D01F9/08Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
    • D01F9/12Carbon filaments; Apparatus specially adapted for the manufacture thereof
    • D01F9/14Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments
    • D01F9/20Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products
    • D01F9/21Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products from macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F9/22Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from polyaddition, polycondensation or polymerisation products from macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyacrylonitriles

Abstract

A METHOD OF STABILIZING ACRYLONITRILE POLYNER FIBERS PRIOR TO CARBONIZATION OR DIRECT GRAPHITIZATION IS DESCRIBED. THE METHOD COMPRISES THE STEP OF HEATING THE FIBERS AT 365-290*C., PERFERABLY AT 275*C., IN AN OXIDIZING ATMOSPHERE FOR, FOR EXAMPLE, ABOUT 3-7 HOURS, IN A MANNER SUCH AS TO DISSIPATE THE HEAT OF REACTION AND ALLOW CONTROLLED OXIDATION. THE STABILIZATION STEP WHEN FOLLOWED BY GRAPHITIZATION OF A POLYMER FIBER OR YARN AT A TEMPERATURE WITHIN THE RANGE OF 1800-3200*C. LEADS TO A GRAPHITE FIBER OF HIGH TENSILE STRENGTH, HIGH MODULUS OF ELASTICITY, AND A FIBER OF IMPROVED GRAPHITIC CHARACTER.

Description

United States Patent 01 fice 3,671,192 Patented June 20, 1972 3,671,192 METHOD OF STABILIZING ACRYLIC POLYMER FIBERS PRIOR TO GRAPHITIZATION Herbert M. Ezekiel, Dayton, Ohio, assignor to the United States of America as represented by the Secretary of the Air Force No Drawing. Filed May 28, 1968, Ser. No. 732,514 The portion of the term of the patent subsequent to Jan. 18, 1972, has been disclaimed Int. Cl. C01b 31/07 US. Cl. 23209.1 9 Claims ABSTRACT OF THE DISCLOSURE A method of stabilizing acrylonitrile polymer fibers prior to carbonization or direct graphitization is described. The method comprises the step of heating the fibers at 265-290 C., preferably at 275 C., in an oxidizing atmosphere for, for example, about 3-7 hours, in a manner such as to dissipate the heat of reaction and allow controlled oxidation. The stabilization step when followed by graphitization of a polymer fiber or yarn at a temperature within the range of 1800-3200 C. leads to a graphite fiber of high tensile strength, high modulus of elasticity, and a fiber of improved graphitic character.
The invention described herein may be manufactured and used by or for the United States Government for governmental purposes without payment to me of any royalty thereon.
BACKGROUND OF THE INVENTION The present invention deals with the stabilization of acrylonitrile polymer fibers and more particularly acrylonitrile polymer yarns. The invention is particularly concerned with such stabilization as a step prior to the subsequent graphitization of the fibers or yarns.
There has been an increasing demand for materials of construction of high strength to weight ratio and high modulus to weight ratio for use in aerospace vehicles and devices; particularly for materials which, additionally, have good thermal stability. Specifically, there has been a demand for improved reinforcing fibers to be embodied in structural composites which form the components of the leading edges of high speed aircraft, the nose cones or heat shields for re-entry vehicles, rocket engine components, and the like.
Graphite and other carbon forms have already been used in reinforcing agents in such structures, and, in particular, have been used in the form of graphite strands or fibers in the reinforcement of composite materials for aerospace structures. Such fibers have been made in a number of ways. An early type of fiber comprised Whiskers resulting from the partial oxidation of natural gas. Another early type of carbon fiber was made by the carbonization of strands of cellulosic material such as strands of cotton. As the plastic field developed many of the new synthetic polymers were substituted for cotton with advantage. Simple carbonization of such fibers, however, led to the production of very weak fibers with practically no resistance to mechanical stresses. Research was then directed to the improvement of the physical properties of the fibers.
An almost invariable practice in the art has been for multiple step, particularly three step, treatment of synthetic polymer yarns. The three step treatment can be defined as: first, a stabilization step which can include oxidation, cross-linking, cyclization, and other well-known polymer reactions and degradations for the temperature range involved; second, a carbonization step which converts the altered high molecular weight polymer fiber to a fiber consisting of a highly carbonaceous residue with as much as several percent each of various elements such as hydrogen, oxygen, nitrogen, and phosphorus depending upon the original polymer nature, the time and temperatures involved in the carbonization process, and the mode of stabilization preceding carbonization; and, third, a graphitization step.
The terms stabilization and stabilized are used herein to describe fibers which have been treated so as to be particularly suitable for graphitization without rupturing or forming large voids or hollow structures during the process. Such stabilized fibers are normally characterized by their increased oxygen content, their uniformity of color in cross sections thereof, and by the integrity of the fibers at all processing stages (that is, they dont stick together).
Graphitization is referred to by the practitioners of this art in the sense of a high temperature treatment, usually above 2000 C.; and it is commonly recognized that this treatment has the effect of yielding materials of almost pure carbon but that the product may or may not be truly graphitic in the crystallographic sense and that the precursor polymer has a pronounced bearing on the degree of graphitic character that one may expect from the treatment. Thus, certain polymers, such as polyvinyl chloride, are called graphitizing and others, such as polyvinylidene chloride and polyacrylonitrile, are called nongraphitizing.
In addition to the division of the graphitization process into these three general steps or temperature ranges the first two steps usually incorporate a gradual heating of the fibers by either utilizing slowly increased temperatures and sometimes holding the fiber at the maximum temperature for that step or utilizing a series of temperatures within the particular step and holding the fibers for various times at each of these temperatures. Thus, French Patent 1,430,803 (Jan. 24, 1966) teaches that polyacrylonitrile fibers are oxidized in the first of a three step process by heating the fiber at about 220 C. for 24 hours in an oxidizing atmosphere, while holding the yarns under tension. Such low temperature pretreatment of the fiber in an oxidizing atmosphere is designed to prepare, or stabilize, the fiber for subsequent carbonization although the patent does not specifically state such a purpose. The patent also describes carbonization processes for these fibers which require 24 to 66 hours for the gradual heating to the maximum carbonization temperature of 1000" C. Similarly, US. Patent 3,107,152 teaches that fiexible fibrous graphite may be produced from cellulosic material by slowly heating the material to about 400 C. during 6 to 30 hours, followed by a heating schedule of about 5 hours to reach a temperature of 900 C. and a subsequent graphitization step.
As indicated above, the workers in the art have stabilized synthetic polymer fibers in a number of ways prior to a second step of carbonizing the fibers at some relatively intermediate temperature and a third step of graphitizing the carbonized fiber at some relatively high temperature.
Despite these improvements in the art, however, the need continues for high strength, high modulus reinforcing fibers for the preparation of structural composites.
OBJECTS It is, therefore, an object of this invention to provide a method for the improvement of the pre-treatment, or stabilization, of acrylonitrile polymer fibers prior to subjecting the latter to carbonization or graphitization.
It is a further object to stabilize such fibers, preferably in the form of yarn, in a manner such that, upon subsequent direct graphitization of the fibers, fibers of improved graphitic character are formed.
3 SUMMARY OF THE INVEN'IlIO N I have now found that the foregoing and related objects can be attained by the method of stabilizing acrylic polymer fibers which comprises the step of heating said fibers at 265-290 C., preferably at 275 C., in an oxidizing atmosphere. I prefer that the fiber be in the form of a yarn and that it be treated in a fashion which will approximately hold the fiber at its original length or cause it to stretch a few percent of its length during stabilization. This latter can be accomplished by using a tension selected to suit the particular yarn or, conveniently, by winding the yarn on a cylinder at a specific, uniform tension.
As indicated previously, the invention finds unique advantage when used as a step prior to the step of direct graphitization. With respect to direct graphitization, I describe in a copending application filed the same date herewith the direct graphitization of a stabilized acrylonitrile polymer fiber by rapidly bringing the stabilized fiber to a high temperature in the range of 18-0O 3200 C., that is without going through any intermediate gradual or prolonged increase in temperature as an intermediate step. Thus, one can obtain a fiber of improved graphitic character by (1) stabilizing the acrylic fiber by the method of this invention and (2) rapidly bringing the stabilized fiber to a high temperature by my new improved method of direct graphitizing stabilized fibers as disclosed and covered in my said copending'application.
The temperature range of 265-290 C. is fairly critical. I believe the superior stabilization results achieved in that temperature range may be due to (l) the attainment of a relatively high temperature without eifecting any significant exothermic decomposition reactions in the acrylic polymer as generally occur at various temperatures above 200 C. depending on the precise acrylic polymer, the size of the polymer sample, and the heat dissipation characteristics of the sample package and the heating method; (2) the effecting of complete stabilization throughout the diameter of the fiber in a reasonably short time (in contrast to times required at 220 C.), for example, in about 7 hours for yarns comprised of 3.75 denier filaments and in about 3-5 hours for yarns comprised of 1.2-2.1 denier filaments; (3) the attainment of a favorable degree of oxidation, or oxygen pick-up (typically about -20 percent by weight) concurrent with the other reactions, especially cyclization and aromatization, which are believed to occur under these conditions; (4) and the attainment of a highly favorable balance between the degree of oxidation of the polymer and the amount of rigidization of the fiber structure (due to cross-linking or analogous processes) which, during a graphitization step, stabilizes the fiber against rupture, pore or void formation, and the like while still imparting to it the strength necessary to allow a wide range of tensions to be used during graphitization. I believe that this last item above allows me to impart to the fiber a higher degree of orientation during the graphitization than is possible with samples stabilized at either lower temperatures (such as 220 C.) or at higher temperatures (such as 300 C.) and it has been shown that a wide range of tensile properties and fiber densities can be achieved by the different tensioning weights and temperatures used with yarns stabilized in this fashion.
The acrylonitrile polymer fibers and yarns used in the method of the invention can be homopolymers, copolymers, terpolymers, graft polymers, and the like of acrylonitrile. I prefer acrylonitrile homopolymers and copolymers such as the copolymer of acrylonitrile and methyl acrylate. In the case of copolymers, for example, these may include nonacrylic constituents. For example, I prefer the copolymer of 97 percent acrylonitrile and 3 percent vinyl acetate and the like copolymers which include about 85 percent or more acrylonitrile units. Typical of such polymers are those sold, for example, under the trademarks Courtelle and Dralon T.
Typical comonomers that can be used are: styrene,
alphamethyl styrene, vinyl toluene, vinyl xylene, vinyl naphthalene, vinyl diphenyl, vinyl methylnaphthalene, vinyl acetate, vinyl chloride, acrylamide, dimethylacrylamide, methacrylonitrile, methyl methacrylate, ethyl acrylate, vinylidene chloride, vinylidene cyanide, phenyl vinyl ether, vinyl methyl phthalate, vinyl methyl maleate, vinyl butyl succinate, ethylene, propylene, butylene, amylene, decylene, etc.
Polymers containing 50% or more acrylonitrile can be used for the purpose of this invention depending on the particular properties desired in the ultimate product. However, for maximum strength properties it is desirable to have at least 65% acrylonitrile and preferably at least acrylonitrile in the starting polymer material.
From the disclosures made herein it should be clear that this invention is successful because provision is made to cope with a well-known phenomenon of acrylonitrile polymers. Usually the buildup of exothermic heat from the oxidation reactions in the polymer sample mass generates a temperature rise which exceeds the so-called explosive exotherm temperature of the particular polymer or copolymer, at which time the sample generally rapidly decomposes to a charred mass. In the practice of this invention, provision should be made to dissipate the heat of reaction so as to allow for controlled oxidation. For example, the sample mass or thickness may be kept small so that air circulation serves this purpose. An alternate method is the winding of single or thin layers of the sample on a metal tube which tends to conduct excess heat away as well as expose the yarn to the circulating air to some degree.
The acrylonitrile polymer fibers are subject to this problem over a wide range of temperatures, at least as low as 220 C. In terms of the advantages of this method of stabilization, improved materials are obtained by utilizing a stabilization temperature range made available because provision is made for the dissipation of the heat of reaction.
In referring to oxidizing atmosphere it is intended that various atmospheres can be used which contain oxygen in such a concentration that the oxidation can be controlled as described herein under the conditions used. Generally atmospheres containing 5-50% oxygen can be used under appropriate conditions, with the remainder of the atmosphere being an inert gas such as nitrogen, argon, helium, etc. Preferably the atmosphere is air.
Suitable tensions on the fibers or yarn during the stabilization step are not critical, although the tension sometimes appears to influence the properties of the stabilized yarn. If the yarn is held under tension by suspended weights or forces along the yarn axis, the weight will be dictated by the requirements for attaining the desired yarn length at the end of the stabilization process. If, on the other hand, the convenient laboratory process of winding the yarn on a cylinder is used, the original elongation and tenacity (strength) properties of the polymer fiber affect both the tensions that can be used on the fiber during stabilization and the orientation that can be incorporated in the stabilized fiber. It is best to avoid placing the yarn under an initial wound tension which is too near the breaking point of the yarn because expansion of the tube upon which the yarn is wound might increase the tension, during the heating step, to beyond the breaking point. It will be apparent that some fibers may be very much weaker than others and it may be necessary to test a specific fiber or yarn before a suitable tension is selected. Generally speaking, increased fiber diameters, increased number of strands, and increased amounts of twist permit high tensions without breaking of the fibers.
Example I A polyacrylonitrile homopolymer yarn consisting of filaments (each 3.75 denier) with no twist is wound on an aluminum tube in a single layer at a tension provided by a 60 gram riding pulley from which a 200 gram weight is suspended. The tube is placed in a circulating air oven for 7 hours at 275 C. A length of the resulting stabilized yarn is then passed through a vertical induction furnace susceptor in an argon atmosphere at 2800 C. under a tension provided by suspending 50 grams from the yarn. The yarn is moved at /2 inch per minute and the hot zone of the susceptor is about /2 inch resulting in the yarn being exposed to the 2800 C. temperature for about one minute. The single filament tensile strength of the resulting fibers is about 265,000 lbs. per square inch and the initial molulus is 61,000,000 lbs. per square inch. X-ray diffraction studies show that the yarn has a high degree of graphitic character.
Example II The foregoing example is repeated except that the high temperature step is carried out under 100 gram tension and the final temperature is 2500 C. The resulting single filament tensile strength is 277,000 lbs. per square inch and the initial modulus is 52,000,000 lbs. per square inch.
Example III Example I is repeated except that the high temperature step is carried out with the yarn under 50 grams tension and moving through a hot zone of about 3000 C. at a rate of 2 inches per minute. The resulting tensile strength of a single filament is 151,000 lbs. per square inch and the intial modulus is 40,000,000 lbs. per square inch.
Example IV A yarn, comprising a copolymer of 94 percent acrylonitrile and 6 percent methyl acrylate and comprising 750 filaments (each 1.5 denier) with no twist, is wound on an aluminum tube in a single layer at a tension provided by a 60 gram pulley from which a 1200 gram weight is suspended and placed in a circulating air oven for 7 hours at 275 C. Portions of the yarn are then treated as indicated in Table I. 1
TABLE I Tensile Rate, Tension, strength, Modulus, Temp., C in./rnin. gms. lbs/sq. in. lbs/sq. in.
Portions of the stabilized yarn are also passed through a furnace about 22 inches long at relatively more rapid rates. Results are in accordance with Table II.
An 800 denier yarn (384 filaments, 0.5 turn per inch twist) made from a copolymer of 99.5 percent acrylonitrile and 0.5 percent methyl acrylate is wound on an aluminum tube under a tension provided by a 60 gram riding pulley from which a 50 gram weight is suspended. The tube is placed in a circulating air oven for 5 hours at 275 C. A length of the resulting stabilized yarn is then graphitized at 2800 C. in the manner described in Example I. A length of the stabilized yarn is similarly graphitized except at a temperature of 2215" C. The resulting single filament tests are shown in Table III. As in the case of the preceding examples, X-ray diffraction studies show the resulting yarn to have a high degree of graphitic character.
A polyacrylonitrile homopolymer yarn consisting of 120 filaments (each 3.75 denier) with no twist is wound on a high temperature glass tube (of approximately 96 percent silica content) at a tension provided by a 60 gram riding pulley from which a 50 gram weight is suspended. The tube is placed in a circulating air oven for 7 hours at 275 C. A length of the resulting yarn is then graphitized at 2520 C. and under a tension of 100 grams in the manner described in Example I. The resulting single filament tensile strength is 254,000 lbs. per square inch and the initial modulus is 54,000,000 lbs. per square inch.
Example VII A portion of polyacrylonitrile homopolymer yarn consisting of filaments (each 3.75 denier) is heated on an aluminum tube for 7 hours at 275 C. and is then carbonized. The carbonization is accomplished by passing the yarn through a three-stage furnace in an inert atmosphere such as lamp grade nitrogen at the rate of eighteen inches per minute. Each of the furnace stages 0r zones is approximately 6 inches in length and the zones are maintained at 430 C., 710 C., and 1000 C., respectively. A tension is maintained on the yarn by placing a light Teflon ring from which a 10 gram weight is suspended over the yarn before the pulley at the entrance of the furnace; the yarn shrinks approximately 13.4 percent during carbonization. The carbonized yarn is then graphitized in the manner described in Example I and as indicated in Table IV.
TABLE IV Tensile Rate, Tension, strength, Modulus, Temp., C. in./min. gms. lbs/sq. in. lbs/sq. in.
Example VIII TABLE VI Tensile Yarn Temp., Rate, Tension, strength, Modulus,
listed C. in./min. g-ms. lbs/sq. in. lbs/sq. in.
Example Some of these yarns are tested at higher tensions and are found to break immediately at the lowest weight used for direct graphitization (50 grams) in the examples above. The superiority of the invention described in the prior examples can be seen readily when processing data and resultant tensile and modulus properties are compared.
Thus the tensile strength and modulus for these fibers of Example VIII stabilized according to prior art methods at 220 C. for 40 hours are much inferior to the modulus and to the tensile strength of fibers stabilized by the process of this invention as illustrated in Examples I-VII. The fact that the tensile strengths of the fibers of Example VIII are greater than those in Example VII is explained by the fact that an intermediate carbonization step is used in Example VII while the direct graphitization process of applicants copending application is used in Example VHI.
Example IX The procedure of Example I is repeated a number of times using individually in place of the polymer of that example the following copolymers respectively:
Acrylom'trile-styrene 80-20 Acrylonitrile-vinyl chloride 85-15 Acrylonitrile-vinylidene chloride 90-10 Acrylonitrile-acrylamide 75-25 Acrylonitrile-methacrylonitrile 50-50 Acrylonitrile-styrene-acrylamide 80-10-10 Acrylonitrile-methyl methacrylate 60-40 Acrylonitrile-vinyl chloride-vinylidene chloride 50-25-25.
In each case improvements in the tensile strength and modulus are noted as compared to the same copolymer stabilized according to prior art method of Example VIII.
The expression oxidizing atmosphere as used herein is intended to include air and other atmospheres containing oxygen in a proportion to give an oxidizing effect somewhat equivalent to air.
While certain features of this invention have been described in detail with respect to various embodiments thereof, it will, of course, be apparent that other modifications can be made within the spirit and scope of this invention and it is not intended to limit the invention to the exact details shown above except insofar as they are defined in the following claims.
I claim:
1. In the process for the high temperature graphitization ofacrylonitrile polymer fibers to form high tensile strength, high modulus of elasticity graphite fibers, the improvement in stabilizing said acrylonitrile polymer fibers prior to graphitization which comprises the step of oxidizing said acrylonitrile polymer fibers by initially heating said polymer fibers at 265 C.-290 C. in an oxygen-containing atmosphere for a period of at least 3 hours, said oxidizing step being conducted with said polymer fibers wound on a metal tube so as to dissipate heat of reaction generated during the oxidation and thereby prevent heat build-up in said acrylonitrile polymer fibers.
2. The process of claim 1 wherein said heating is at a temperature of about 275 C.
3. The method according to claim 1 wherein said fibers are in the form of a yarn and are under tension.
4. The process of claim 1 wherein said fibers are in the form of yarn, areunder tension, and said heating is continued for about 3-7 hours.
5. The process of claim 1 wherein said polymer comprises an acrylonitrile copolymer containing at least percent by weight of acrylonitrile.
6. The process of claim 1 wherein said polymer comprises an acrylonitrile homopolymer.
7. The process of claim 1 wherein said polymer is a copolymer of methyl acrylate and at least 50 percent by weight of acrylonitrile.
8. The process of claim 1 wherein said polymer is a copolymer of about 97 percent by weight acrylonitrile and about 3 percent by weight vinyl acetate.
9. The process of claim 1 wherein said polymer is a copolymer having at least percent by weight of acrylonitrile.
References Cited UNITED STATES PATENTS 2,799,915 7/1957 Barnett et al -8115.5 X 3,285,696 11/1966 Tsunoda 23209.1 3,399,252 8/1968 Hough et al. 23-2093 3,412,062 11/196 8 Johnson et a1. 23209.1 UX 3,449,077 6/ 1969 Stuetz 23209.1 3,508,874 4/ 1970 Rulison 23-209.1
FOREIGN PATENTS 911,542 11/1962 Great Britain 23-2091 OTHER REFERENCES Vosburgh: Textile Research Journal, vol. 30, 1960, pp. 882-896.
EDWARD J. MEROS, Primary Examiner US. Cl. X.R.
fi ITED Si s PATENT. OFF-ICE. Y
CERTIFICATE Q OR EQTIQ [Par nt'No.,**3;671,19 I ma. June 197 xn ventms Herbert M. Ezekiel It iscertif'ie d that error appears in. the above-identified patent and that said Letters Patent are herebyeorrected as shown below:
i"'('Jo1\. 1mri- 1, "line 9,' "Ja-n'.' 18, 1972 should read Jan. 18, 1989 iSi'gne d and sealed this 2Znd d'ay of May 1973.
I E qAttest'z' I IIYI'EIDWARD M-.FL'ETCHER,JR. 1; ROBERT 5OTTSCHALK I .TA-tt e sting "Officer-3 I COIIIIIIILSSIOIIGIIZ of Patents y
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3841079A (en) * 1970-04-14 1974-10-15 Celanese Corp Carbon filaments capable of substantial crack diversion during fracture
US3886263A (en) * 1972-02-03 1975-05-27 Agency Ind Science Techn Method for manufacture of heat-resistant fibers
US3971840A (en) * 1973-03-27 1976-07-27 The Carborundum Company Production of high strength carbide fibers by heat treatment
US3976729A (en) * 1973-12-11 1976-08-24 Union Carbide Corporation Process for producing carbon fibers from mesophase pitch
US3993950A (en) * 1975-06-06 1976-11-23 Piltingsrud Harley V Carbon fiber electrometer for dosimeter
US4005183A (en) * 1972-03-30 1977-01-25 Union Carbide Corporation High modulus, high strength carbon fibers produced from mesophase pitch
US4065549A (en) * 1974-10-21 1977-12-27 Toray Industries, Inc. High tensile strength, high Young's modulus carbon fiber having excellent internal structure homogeneity, and process for producing the same
US4077822A (en) * 1976-11-17 1978-03-07 Celanese Corporation Splice for use during the thermal stabilization of a flat multifilament band of an acrylic fibrous material comprising at least two segments
US4080413A (en) * 1975-12-15 1978-03-21 United Technologies Corporation Porous carbon fuel cell substrates and method of manufacture
USRE30414E (en) * 1974-10-21 1980-10-07 Toray Industries, Inc. Process for producing a high tensile strength, high Young's modulus carbon fiber having excellent internal structure homogeneity
US4256607A (en) * 1976-10-05 1981-03-17 Toho Beslon Co., Ltd. Process for production of activated carbon fibers
US4285831A (en) * 1976-10-05 1981-08-25 Toho Beslon Co., Ltd. Process for production of activated carbon fibers
US4336022A (en) * 1979-08-01 1982-06-22 E. I. Du Pont De Nemours And Company Acrylic precursor fibers suitable for preparing carbon or graphite fibers

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3841079A (en) * 1970-04-14 1974-10-15 Celanese Corp Carbon filaments capable of substantial crack diversion during fracture
US3886263A (en) * 1972-02-03 1975-05-27 Agency Ind Science Techn Method for manufacture of heat-resistant fibers
US4005183A (en) * 1972-03-30 1977-01-25 Union Carbide Corporation High modulus, high strength carbon fibers produced from mesophase pitch
US3971840A (en) * 1973-03-27 1976-07-27 The Carborundum Company Production of high strength carbide fibers by heat treatment
US3976729A (en) * 1973-12-11 1976-08-24 Union Carbide Corporation Process for producing carbon fibers from mesophase pitch
US4065549A (en) * 1974-10-21 1977-12-27 Toray Industries, Inc. High tensile strength, high Young's modulus carbon fiber having excellent internal structure homogeneity, and process for producing the same
USRE30414E (en) * 1974-10-21 1980-10-07 Toray Industries, Inc. Process for producing a high tensile strength, high Young's modulus carbon fiber having excellent internal structure homogeneity
US3993950A (en) * 1975-06-06 1976-11-23 Piltingsrud Harley V Carbon fiber electrometer for dosimeter
US4080413A (en) * 1975-12-15 1978-03-21 United Technologies Corporation Porous carbon fuel cell substrates and method of manufacture
US4256607A (en) * 1976-10-05 1981-03-17 Toho Beslon Co., Ltd. Process for production of activated carbon fibers
US4285831A (en) * 1976-10-05 1981-08-25 Toho Beslon Co., Ltd. Process for production of activated carbon fibers
US4077822A (en) * 1976-11-17 1978-03-07 Celanese Corporation Splice for use during the thermal stabilization of a flat multifilament band of an acrylic fibrous material comprising at least two segments
US4336022A (en) * 1979-08-01 1982-06-22 E. I. Du Pont De Nemours And Company Acrylic precursor fibers suitable for preparing carbon or graphite fibers

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