US3454362A - Process for producing fibrous graphite - Google Patents

Process for producing fibrous graphite Download PDF

Info

Publication number
US3454362A
US3454362A US483395A US3454362DA US3454362A US 3454362 A US3454362 A US 3454362A US 483395 A US483395 A US 483395A US 3454362D A US3454362D A US 3454362DA US 3454362 A US3454362 A US 3454362A
Authority
US
United States
Prior art keywords
yarn
temperature
filament
stretching
elongation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US483395A
Inventor
William J Spry
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BP Corp North America Inc
Original Assignee
Union Carbide Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Union Carbide Corp filed Critical Union Carbide Corp
Application granted granted Critical
Publication of US3454362A publication Critical patent/US3454362A/en
Anticipated expiration legal-status Critical
Assigned to AMOCO CORPORATION, A CORP. OF INDIANA reassignment AMOCO CORPORATION, A CORP. OF INDIANA ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: UNION CARBIDE CORPORATION
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • 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
    • D01F9/16Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from products of vegetable origin or derivatives thereof, e.g. from cellulose acetate
    • 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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S264/00Plastic and nonmetallic article shaping or treating: processes
    • Y10S264/19Inorganic fiber

Definitions

  • the present invention relates to an improved process for the production of filaments or yarn from carbonized polymeric fibrous materialsand to the filaments and yarn so produced.
  • the individual monofilaments of the thus treated or graphitized material have a tensile strength of up to 100,000 pounds per square inch. While the individual filaments possess such strength, the yarns made from a plurality of the same filaments and treated under the same conditions have a tensile strength of only approximately 15,000 pounds per square inch.
  • the principal object of the present invention is to provide a method of producing a high temperature refractory filament or yarn from a carbonized polymeric filament or yarn, the produced material having improved physical properties such as an increased Youngs modulus and an improved tensile strength.
  • Another object of the present invention is to provide a method of increasing the Youngs modulus and tensile 2 strength of the individual monofilaments which make up a length of graphite yarn.
  • Still another object of the present invention is to provide a graphite yarn having a tensile strength more commensurate with the tensile strength of the individual monofilaments which make up the yarn.
  • the present invention provides a process for producing an improved high temperature refractory filament or yarn which comprises heating a carbonaceous polymeric filament or yarn to a temperature sufficient to permit plastic 0w and longitudinally stretching the heated filament or yarn by subjecting said heated filament or yarn to a tensional force until an elongation of at least about 1% of the original length of the filament or yarn has been obtained. While in the case of yarn, a significant improvement is shown after a stretch of only 1%, in the case of an individual monofilament a stretch of the order of about 10% is required before significant improvements in the properties are clearly in evidence.
  • the present invention also provides an improved high temperature refractory yarn of cellulosic origin formed of a plurality of monofilaments having a Youngs modulus of more than 10X 10 lb./in. and a breaking strength of more than 12 10 lb./in.
  • a yarn of cellulosic origin has been produced wherein the individual monofilaments have a Youngs modulus of the order of 55 10 lb./in. and a breaking strength of the order of 36.5)(10 lb./in.
  • FIGURE 1 is an electron micrograph having a magnification factor of 93,000 of a thin slice of an unstretched rayon filament which has been subjected to graphitizing temperatures.
  • the plane of the slice is parallel to the filament axis.
  • the grain of this structure is parallel to the filament axis, but the orientation is not very pronounced.
  • FIGURE 2 is an electron micrograph having a magnification factor of 138,000 of a thin slice of a rayon filament which has been subjected to a graphitizing temperature and stretched by the process of the invention.
  • the plane of the slice is parallel to the filament axis.
  • the grain of this structure is also parallel to the filament axis and as compared to FIGURE 1, the orientation is very pronounced.
  • the filament of FIGURE 2 had a Youngs modulus of 55 X 10 lb./in. The significance of this high degree of orientation will be fully discussed hereinafter.
  • carbonaceous yarn is intended to cover a yarn which has already been graphitized in a separate operation and is thereafter subjected to the process of the present invention, as well as a carbon yarn which is a yarn having been carbonized by being heated up to a carbonizing temperature but below graphitizing temperatures and which is therefore simultaneously treated to higher temperatures which are commonly recognized as graphitizing and stretched by the process of the present invention.
  • the yarns suitable for use in the process of the present invention include carbon and graphite yarns produced by carbonizing polymeric, fibrous materials such as polyacrylonitrile, polyvinyl alcohol, and natural and preferably regenerated cellulose.
  • the temperature at which the monofilaments of the yarn show a significant degree of plasticity varies according to the nature and origin of the yarn; with yarns of cellulosic origin it has been observed that stretching under a tensional force begins at a temperature in the vicinity of the maximum temperature of the previous heat-treatment to which the material has been subjected. For example, stretching of a carbon yarn under load will begin at approximately 1200 C., whereas no stretching of a pre-graphitized yarn will take place at a temperature much below 2300 C. However, significant stretching of the carbon yarn will not begin at a temperature of less than 1500 C. and a minimum temperature of 2500 C. is necessary to obtain significant stretching of the pregraphitized yarn.
  • the maximum temperature at which the process of the present invention may be carried out is not critical. It should be kept below the temperature of vaporization of graphite, i.e., approximately 3600 C.
  • a high temperature induction furnace was constructed for stretching carbonaceous yarns at elevated temperatures according to the process of the present invention. It consisted of a hollow, cylindrical graphite susceptor which was inductively heated by a conventional induction coil, a graphite support rod positioned across the top of the susceptor for mounting the sample, and a system for providing an inert atmosphere in the hot zone of the assembly.
  • a carbon yarn sample (single ply, 637 denier with 720 filaments per ply) of regenerated cellulose which had previously been carbonized at a maximum temperature of 1300 C., was doubled over and passed through the apparatus. The yarn was joined together at the two ends and a weight was attached thereto which thereby put the sample under tension.
  • the susceptor was heated by gradually increasing the power and the yarn was, accordingly, heated by radiation from the susceptor. When the temperature within the hot zone reached about 1200 C. the yarn began to stretch. The amount of stretch was measured by means of a cathetometer. The final temperature achieved was between 2800 C. and 2830 C. The sample was maintained at this maximum temperature for 25 minutes. The sample was then cooled to room temperature, removed from the apparatus and measured for any change in physical properties.
  • Flaws in the structure of the filament such as internal voids or pits on the external surface of the filament, produce stress concentrations at their extremities when a tension is applied to the filament.
  • the stress concentration will be correspondingly large, and when the applied tension becomes sufficiently large a crack leading to ultimate fracture can develop.
  • the stretching of the filament would cause the radius of curvature at the bottom of the surface pit to increase, and thereby reduce its effectiveness as a stressconcentrator.
  • EMMPLE III A single ply 206 denier graphite yarn consisting of 720 filaments having approximatel 2 twists per inch was tested and found to have an effective yarn tenacity of .81 gram per denier: (corresponding to an actual effective breaking load of 167 grams). Based on actual tensile strength tests on individual filaments, the theoretical maximum tenacity of this yarn is calculated to be 7.15 grams/ denier. A span of this yarn corresponding to a free length of 0.9 inch was mounted in a small jig constructed from parts machined from structural graphite.
  • the mechanical design of the jig was such that a tensile load of a known amount could be applied to the yarn sample by means of a fixed weight and the amount of elongation taking place over the sample length could be limited to a predetermined amount by means of a support rod having a calibrated thread under the weight.
  • the entire assembly was installed within a 4 inch diameter graphite tube which could be heated electrically to graphitizing temperatures. After flooding the interior of the graphite tube with argon, the tube and assembly with the yarn sample supporting a tensile load of 40 grams (corresponding to .2 gram/ denier) was heated rapidly to 2800 C. and held at that temperature for approximately 5 minutes and the tube furnace was then allowed to cool rapidly.
  • This example shows the improvement in the treated yarn, obtained by relieving unequal filament-to-filament stresses in said yarn and orienting the crystallites in the graphitic layers in a direction parallel to the longitudinal axis of each monofilament with the resulting improved properties of the individual filaments of the yarn.
  • a process for producing an improved high temperature refractory yarn which comprises heating in a protective atmosphere a carbonaceous yarn in graphite form up to a temperature suflicient to permit plastic flow and longitudinally stretching the heated yarn by subjecting said heated yarn to a tensional force until an elongation of at least 1% of the original length of the yarn has been obtained, and cooling the permanently elongated yarn.
  • a process for producing an improved high temperature refractory yarn which comprises heating a carbonaceous yarn in a carbonized form in a protective atmosphere to a graphitizing temperature sufiicient to permit plastic flow and longitudinally stretching the heated yarn by subjecting said heated yarn to a tensional force until an elongation of at least 1% of the original length of the yarn has been obtained, and cooling the permanently elongated yarn.
  • a process for producing an improved high temperature refractory monofilament which comprises heating a carbonaceous monofilament in graphite form to a temperature suflicient to permit plastic flow and longitudinally stretching the heated monofilament by subjecting said monofilament to a tensional force untilan elongation of at least about 10% of the original length of the monofilament has been obtained, and cooling the permanently elongated monofilament.
  • the carbonaceous yarn is provided by subjecting to a carbonizing environment a yarn selected from the group consisting of polyacrylonitrile, polyvinyl alcohol and natural and regenerated cellulose.
  • a process for producing an improved high temperature refractory monofilament which comprises heating a carbonaceous monofilament in a carbonized form to a graphitizing temperature suflicient to permit plastic flow and longitudinally stretching the heated monofilament by subjecting said monofilament to a tensional force until an elongation of at least about 10% of the original length of the monofilament has been obtained, and cooling the permanently elongated monofilament.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Inorganic Fibers (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)

Description

July 8, 1969 W. J. SPRY 3,454,362
PROCESS FOR PRODUCING FIBROUS GRAPHITE Filed Aug. 26, 1965 Sheet of 2 INVENTOR. WILLIAM J.SPRY
" awm July 8, 1969 Filed Aug.
w. J. SPRY 3,454,362
PROCESS FOR PRODUCING FIBROUS GRAPHITE Sheet Z of2 INVENTOR. WILLIAM J. SPRY United States Patent Office 3,454,362 Patented July 8, 1969 3,454,362 PROCESS FOR PRODUCING FIBROUS GRAPHITE William J. Spry, North Olmsted, Ohio, assignor to Union Carbide Corporation, a corporation of New York Continuation-impart of application Ser. No. 157,259, Dec. 5, 1961. This application Aug. 26, 1965, Ser. No. 483,395 Claims priority, application Great Britain, Mar. 16, 1965, 11,022/ 65 Int. Cl. C01b 31/04 US. Cl. 23-2091 9 Claims ABSTRACT OF THE DISCLOSURE This application is a continuation-in-part of application Ser. No. 157,259, filed Dec. 5, 1961, now abandoned.
The present invention relates to an improved process for the production of filaments or yarn from carbonized polymeric fibrous materialsand to the filaments and yarn so produced.
It is known to subject to graphitizing temperatures cellulosic fibrous material such as cloth, felt, braids, yarns, knits and weaves by subjecting them to a controlled heating schedule which comprises a slow heating stage at a temperature of from 100 C. to 300 C. at a rate of increase of up to 50 C. per hour, followed by a second heating stage from 300 C. to 400 C. in which the temperature is increased at a rate of up to 55 C. per hour, then heating to cause the temperature to increase at a rate of up to 100 C. per hour at temperatures up to 900 C. From 900 C. until the treatment is complete, at around 3000 C., rapid heating rates of up to 3000 C. per hour may be employed.
The individual monofilaments of the thus treated or graphitized material have a tensile strength of up to 100,000 pounds per square inch. While the individual filaments possess such strength, the yarns made from a plurality of the same filaments and treated under the same conditions have a tensile strength of only approximately 15,000 pounds per square inch.
When it is considered that during the described process the individual filaments within the twisted yarn undoubtedly undergo unequal shrinkage, this discrepancy in strength is not surprising. With unequal shrinkage from filament to filament, unequal residual strains are bound to exist. When a yarn is stressed uniformly, the shorter filaments are the first to be strained. The elongation prior to breaking in a manufactured graphite filament has be n found to be less than 1% at room temperature, and the shorter filaments break before the strain can be distributed equally throughout the yarn.
The principal object of the present invention is to provide a method of producing a high temperature refractory filament or yarn from a carbonized polymeric filament or yarn, the produced material having improved physical properties such as an increased Youngs modulus and an improved tensile strength.
Another object of the present invention is to provide a method of increasing the Youngs modulus and tensile 2 strength of the individual monofilaments which make up a length of graphite yarn.
Still another object of the present invention is to provide a graphite yarn having a tensile strength more commensurate with the tensile strength of the individual monofilaments which make up the yarn.
These objects are achieved by heating a carbonaceous polymeric filament or yarn to a temperature high enough to cause the filament or the individual monofilaments forming the yarn to reach a degree of plasticity which allows them ,to be stretched when the yarn is subjected to a tensional force, while in such a plastic condition and to remain permanently stretched after cooling of the filament or yarn. The heating and stretching is done in anatmosphere which protects the material from being oxidized. An inert atmosphere, such as argon, has been found very suitable for this purpose.
Accordingly, the present invention provides a process for producing an improved high temperature refractory filament or yarn which comprises heating a carbonaceous polymeric filament or yarn to a temperature sufficient to permit plastic 0w and longitudinally stretching the heated filament or yarn by subjecting said heated filament or yarn to a tensional force until an elongation of at least about 1% of the original length of the filament or yarn has been obtained. While in the case of yarn, a significant improvement is shown after a stretch of only 1%, in the case of an individual monofilament a stretch of the order of about 10% is required before significant improvements in the properties are clearly in evidence.
The present invention also provides an improved high temperature refractory yarn of cellulosic origin formed of a plurality of monofilaments having a Youngs modulus of more than 10X 10 lb./in. and a breaking strength of more than 12 10 lb./in. By utilizing the optimum process conditions a yarn of cellulosic origin has been produced wherein the individual monofilaments have a Youngs modulus of the order of 55 10 lb./in. and a breaking strength of the order of 36.5)(10 lb./in.
In order that the degree of orientation achieved by the process of the invention be fully illustrated, reference will be had to the drawing, the figures of which are electron micrographs of unstretched and stretched filaments.
More specifically, FIGURE 1 is an electron micrograph having a magnification factor of 93,000 of a thin slice of an unstretched rayon filament which has been subjected to graphitizing temperatures. The plane of the slice is parallel to the filament axis. The grain of this structure is parallel to the filament axis, but the orientation is not very pronounced.
FIGURE 2 is an electron micrograph having a magnification factor of 138,000 of a thin slice of a rayon filament which has been subjected to a graphitizing temperature and stretched by the process of the invention. The plane of the slice is parallel to the filament axis. The grain of this structure is also parallel to the filament axis and as compared to FIGURE 1, the orientation is very pronounced. The filament of FIGURE 2 had a Youngs modulus of 55 X 10 lb./in. The significance of this high degree of orientation will be fully discussed hereinafter.
For convenience sake the bulk of the disclosure hereinafter will be directed to the treatment of a yarn made up a plurality of filaments and the yarn so produced. It will be appreciated that the disclosed process is equally applicable to the treatment of a monofilament.
The expression carbonaceous yarn is intended to cover a yarn which has already been graphitized in a separate operation and is thereafter subjected to the process of the present invention, as well as a carbon yarn which is a yarn having been carbonized by being heated up to a carbonizing temperature but below graphitizing temperatures and which is therefore simultaneously treated to higher temperatures which are commonly recognized as graphitizing and stretched by the process of the present invention.
The yarns suitable for use in the process of the present invention include carbon and graphite yarns produced by carbonizing polymeric, fibrous materials such as polyacrylonitrile, polyvinyl alcohol, and natural and preferably regenerated cellulose.
Although the temperature at which the monofilaments of the yarn show a significant degree of plasticity varies according to the nature and origin of the yarn; with yarns of cellulosic origin it has been observed that stretching under a tensional force begins at a temperature in the vicinity of the maximum temperature of the previous heat-treatment to which the material has been subjected. For example, stretching of a carbon yarn under load will begin at approximately 1200 C., whereas no stretching of a pre-graphitized yarn will take place at a temperature much below 2300 C. However, significant stretching of the carbon yarn will not begin at a temperature of less than 1500 C. and a minimum temperature of 2500 C. is necessary to obtain significant stretching of the pregraphitized yarn. In addition, the closer the temperature at which the stretching is done is to the maximum temperature to which the material was previously subjected, the longer the time required at a given temperature within the indicated range to achieve the same improvement in properties. The maximum temperature at which the process of the present invention may be carried out is not critical. It should be kept below the temperature of vaporization of graphite, i.e., approximately 3600 C.
The present invention will now be further described in the following examples.
EXAMPLE I A high temperature induction furnace was constructed for stretching carbonaceous yarns at elevated temperatures according to the process of the present invention. It consisted of a hollow, cylindrical graphite susceptor which was inductively heated by a conventional induction coil, a graphite support rod positioned across the top of the susceptor for mounting the sample, and a system for providing an inert atmosphere in the hot zone of the assembly. A carbon yarn sample (single ply, 637 denier with 720 filaments per ply) of regenerated cellulose which had previously been carbonized at a maximum temperature of 1300 C., was doubled over and passed through the apparatus. The yarn was joined together at the two ends and a weight was attached thereto which thereby put the sample under tension. The susceptor was heated by gradually increasing the power and the yarn was, accordingly, heated by radiation from the susceptor. When the temperature within the hot zone reached about 1200 C. the yarn began to stretch. The amount of stretch was measured by means of a cathetometer. The final temperature achieved was between 2800 C. and 2830 C. The sample was maintained at this maximum temperature for 25 minutes. The sample was then cooled to room temperature, removed from the apparatus and measured for any change in physical properties.
Four experiments were carried out with four identical yarns in the conditions above described. The only difference was in the weight of the load attached to the sample, which was 50 gm., 400 gm., 800 gm. and 1400 gm., respectively. Stretching or elongation of the samples increased with increasing load attached to the yarn.
It could be seen that a measurable amount of elongation occurred even for very small loads. Some of this elongation was reversible as it was due to the thermal expansion of the fibers while the remaining position of the elongation was permanent as it was due to an actual stretching or lengthening of the fibers themselves. Any elongation which occurred beyond the purely heat-treatment-induced elongation is called stress-induced elonga- 4 tion, or stretching and is permanent in nature. It is only the stress-induced elongation which accounts for the improvement of the properties under discussion as reported in Table 1.
As a result of the permanent stretch applied to these samples, marked increases were found in strength and Youngs modulus, measured on individual filaments. Individual filaments were tested in tension at room temperature with an Instrom testing machine. For each stretched sample tested, at least 10 measurements of strength and Youngs modulus were made. The average cross-sectional area of individual filaments for each yarn sample tested were obtained by direct measurements of at least twenty representative individual filaments taken from the yarn sample. Results of these measurements are shown in Table 1 below. The average cross-sectional area, Youngs modulus and breaking strength of the individual filaments of the initial carbon yarn samples were also measured and are shown in Table 1. For comparison purposes, the properties of a graphite filament produced by the known heating schedule previously mentioned are also listed in Table 1. It should be understood that the percent elongation given in the table for the monofilaments is substantially equal to the percent elongation occurred in the yarn upon stretching. The actual percentage figures in Table 1 represent the inverse ratio of the cross sections of the filament before and after stretching, and this figure closely approximates the percent elongation.
TAB LE 1 Properties of Initial Canbonized Filament (maximum processing temperature 1,300 0.)
Properties of prior art graphite filament (maximum processing temperature 2,800 C.)
Properties of filaments from carbon yarns stretched under tensile loads during heating to a temperature of 2,800 C. to 2,830 O.
*Range.
Since the yarn sample heated under a load of 50 gm. was found to stretch only very slightly, this sample showed properties which are substantially equivalent to the properties to be expected from a yarn sample heated under zero load. Comparison of the properties of the sample heated under a load of 1400 gm. with that of the 50 gm. sample, shows that the eifect of stretching the yarn under a load of 1400 gm. was to produce nearly a 6-fold increase in Youngs modulus and a 3 /2-fold increase in breaking strength of individual filaments taken from the yarn. It should be pointed out that there is no absolute limit on the amount stretch which may be imparted to a filament or yarn by the process of the invention other than a practical one, i.e., the stress employed to impart the stretch must not exceed the stress which the material can withstand at each given point in time.
The explanation for the remarkable changes in properties lies first in the fact that one result of the stretching was the partial alignment of graphitic or graphitic-like layers into positions characterized by preferential orientation of layers parallel to the filament axis. That this effect had occurred was shown conclusively through examination of X-ray diffraction fiber patterns. It is well known in carbon and graphite technology, that a carbon material with a high degree of preferred orientation causes a high Youngs modulus when measured parallel to the direction of the oriented layers. The higher the degree of preferred orientation, the higher the Youngs modulus. The cause of this is known to be the high Youngs modulus of crystallites measured along the layers as compared to the modulus measured normal to the layers.
Secondly, with regard to the increase in strength of stretched filaments compared to 'unstretched filaments, there are several probable causes:
(1) The preferential orientation of layers parallel to the filament axis makes it difiicult to propagate incipient cracks within the filament in directions transverse to the axis. This is because cracks can more easily propagate between graphitic layers than across, or through, the layers. Cracks transverse to the axis tend to be propagated by an applied tension, whereas cracks parallel to the axis are not propagated by an applied tension, and are hence ineffective in producing fracture.
(2) Flaws in the structure of the filament, such as internal voids or pits on the external surface of the filament, produce stress concentrations at their extremities when a tension is applied to the filament. In the example of surface pits, if the radius of curvature at the bottom of the pit is small, the stress concentration will be correspondingly large, and when the applied tension becomes sufficiently large a crack leading to ultimate fracture can develop. The stretching of the filament would cause the radius of curvature at the bottom of the surface pit to increase, and thereby reduce its effectiveness as a stressconcentrator.
(3) When a carbon filament is cooled to room temperature from the maximum heat-treatment temperature used in its manufacture or preparation prior to tensile testing, internal stresses are produced due to unequal thermal contractions in adjacent regions within the filament. The cause for these unequal thermal contractions is the difference in thermal expansion coefiicient of crystallites measured parallel to the layers and measured normal to the layers. If adjacent crystallites are oriented in different relations to the filament axis, then unequal thermal contractions will occur and produce internal stresses. These internal stresses, when added to the externally applied tensile stress, will lead to premature fracture. Since the stretching process tends to orient crystallites with their layers parallel to the axis of the filament, there is a reduction in the inducement of internal stresses during cooling and hence an increase in strength.
EXAMPLE II Using the apparatus described in Example I, and under the same conditions of temperature and time, experiments were carried out with a yarn (single ply, 506 denier with 720 filaments per ply) of a regenerated cellulosic origin which had been previously subjected to a graphitizing temperature of 2800 C. A load of 1000 gm. was attached to the yarn sample. While for the carbon yarns of Example I stretching under load had begun at approximately 1200 C., i.e., near the maximum carbonization temperature of the yarns, it was found that no significant stretching of this yarn occurred until approximately 2500 C. which was near the previous graphitizing temperature. At 2500 C. the amount of stretching which occurred was very slight. Only after raising the temperature to 2800 C. did appreciable stretching occur. The amount of stretching that occurred as a result of the increase in temperature from 2500 C. to 2800 C. was similar to that which occurred in the corresponding samples which had not been subjected to pre-graphitizing temperatures as a result of the same increase in temperature from 2500 C. to 2800 C. Therefore the total elongation of the samples treated previously at graphitizing temperatures was much less than that of samples not treated at such high temperatures.
The results of these experiments are shown in Table 2 below. The individual filaments of the samples were measured in the same manner as described in Example I.
6 TABLE 2 Properties of filaments from yarns previously treated at graphitizing temperatures stretched under tensile loads during heating to a temperature of 2800 C.:
Load applied, (g.) 1000 Average cross section area, 10" cm. 50.3 Percent elongation 16 Youngs modulus, 10 lb./in. 13.6 Breaking strength, 10 lb./in. 12.8
It is clear from this second series of experiments that, although the previously high temperature treated yarns do not benefit from heating under load as much as the yarns which have only been pre-carbonized, their individual filaments still show a definite improvement in Youngs modulus and breaking strength over the filaments of prior art graphite yarns.
EMMPLE III A single ply 206 denier graphite yarn consisting of 720 filaments having approximatel 2 twists per inch was tested and found to have an effective yarn tenacity of .81 gram per denier: (corresponding to an actual effective breaking load of 167 grams). Based on actual tensile strength tests on individual filaments, the theoretical maximum tenacity of this yarn is calculated to be 7.15 grams/ denier. A span of this yarn corresponding to a free length of 0.9 inch was mounted in a small jig constructed from parts machined from structural graphite. The mechanical design of the jig Was such that a tensile load of a known amount could be applied to the yarn sample by means of a fixed weight and the amount of elongation taking place over the sample length could be limited to a predetermined amount by means of a support rod having a calibrated thread under the weight. The entire assembly, was installed within a 4 inch diameter graphite tube which could be heated electrically to graphitizing temperatures. After flooding the interior of the graphite tube with argon, the tube and assembly with the yarn sample supporting a tensile load of 40 grams (corresponding to .2 gram/ denier) was heated rapidly to 2800 C. and held at that temperature for approximately 5 minutes and the tube furnace was then allowed to cool rapidly. In the case of one sample, the total stretch was limited to 1% of its free span length. Examination of the cooled testing assembly showed that the yarn sample had reached a plastic stage at a temperature of about 2200 C. and had been permanently stretched. The effect1ve strength of the thus treated yarn was found to be 1.18 grams/denier. In a second experiment under these same conditions with another sample of the same size of yarn a total elongation of 2% was allowed to take place. The effective strengh of this yarn was found to be 1.23 grams/denier.
It will be appreciated from a study of the above figures that untreated graphitized yarn of the prior art has effective strength of only 11% of the theoretical. An elongatron of 1% of the graphitized yarn by the process of the present invention results in an efiective strength equal to 15% of theoretical or approximately a 50% increase. A 2% elongation results in an effective strength of 17% of theoretical. While an elongation of at least 1% of the origlnal length of the yarn is necessary to improve the strength of the yarn, there is practically no upper limit for the elongation. It is obvious from Tables 1 and 2 above, that the strength of the yarns increases with increasing elongation of the yarn.
This example shows the improvement in the treated yarn, obtained by relieving unequal filament-to-filament stresses in said yarn and orienting the crystallites in the graphitic layers in a direction parallel to the longitudinal axis of each monofilament with the resulting improved properties of the individual filaments of the yarn.
7 EXAMPLE 1v Another experiment was performed in which a sample of carbon yarn, which had not been previously subjected to graphitizing temperatures was stretched under a load of 1300 gm. in the conditions described in Example I. The resulting stretched and graphitized yarn was cooled to room temperature, and then subjected a second time to the same heating schedule under the same 1300 gm. load. In the second treatment, no detectable stretching occurred until a temperature of 2800 C. was reached. This experiment points up an obvious benefit of the stretching process of the present invention, namely, that stretching of yarns under high loads at high temperature renders them totally resistant to creep under loads equal to or less than that used in the stretching treatment at all temperatures below the maximum temperature attained during the treatment. This property of resistance to creep is of great importance in structural applications at high temperatures, such as when carbon yarns are used in filament wound structures as the primary load-bearing material.
What is claimed is:
1. A process for producing an improved high temperature refractory yarn which comprises heating in a protective atmosphere a carbonaceous yarn in graphite form up to a temperature suflicient to permit plastic flow and longitudinally stretching the heated yarn by subjecting said heated yarn to a tensional force until an elongation of at least 1% of the original length of the yarn has been obtained, and cooling the permanently elongated yarn.
2. A process for producing an improved high temperature refractory yarn which comprises heating a carbonaceous yarn in a carbonized form in a protective atmosphere to a graphitizing temperature sufiicient to permit plastic flow and longitudinally stretching the heated yarn by subjecting said heated yarn to a tensional force until an elongation of at least 1% of the original length of the yarn has been obtained, and cooling the permanently elongated yarn.
3. The process of claim 2 wherein said heating is done in an argon atmosphere.
4. A process as claimed in claim 1, in which the graphite yarn is of cellulosic origin and heated to a temperature of at least about 25 C.
5. A process as claimed in claim 4 wherein said heating is done in an argon atmosphere.
6. A process as claimed in claim 1, in which the carbonaceous yarn is provided by subjecting to a graphitizing environment a yarn selected from the group consisting of polyacrylonitrile, polyvinyl alcohol and natural and regenerated cellulose.
7. A process for producing an improved high temperature refractory monofilament which comprises heating a carbonaceous monofilament in graphite form to a temperature suflicient to permit plastic flow and longitudinally stretching the heated monofilament by subjecting said monofilament to a tensional force untilan elongation of at least about 10% of the original length of the monofilament has been obtained, and cooling the permanently elongated monofilament.
8. A process as claimed in claim 2 in which the carbonaceous yarn is provided by subjecting to a carbonizing environment a yarn selected from the group consisting of polyacrylonitrile, polyvinyl alcohol and natural and regenerated cellulose.
9. A process for producing an improved high temperature refractory monofilament which comprises heating a carbonaceous monofilament in a carbonized form to a graphitizing temperature suflicient to permit plastic flow and longitudinally stretching the heated monofilament by subjecting said monofilament to a tensional force until an elongation of at least about 10% of the original length of the monofilament has been obtained, and cooling the permanently elongated monofilament.
References Cited UNITED STATES PATENTS 2,263,217 11/1941 Lillie et al. 28-72X 2,509,292 5/1950 Finlayson et al 8-132 X 2,624,934 1/1953 Munson et a1 28-72X 2,957,756 10/ 1960 Bacon 23-2092 3,011,981 12/1961 Soltes 252-502 3,107,152 10/ 1963 Ford et al. 23-2092 3,116,975 1/ 1964 Cross et al 23-2092 X 3,179,605 4/1965 Ohsol 252-502 3,304,148 2/ 1967 Gallagher 23-2092 X 3,285,696 11/1966 Tsunoda 23-209.1
EDWARD J. MEROS, Primary Examiner.
US. Cl. X.R. 23-2092
US483395A 1965-03-16 1965-08-26 Process for producing fibrous graphite Expired - Lifetime US3454362A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB11022/65A GB1093084A (en) 1965-03-16 1965-03-16 Manufactured graphite yarn

Publications (1)

Publication Number Publication Date
US3454362A true US3454362A (en) 1969-07-08

Family

ID=9978622

Family Applications (2)

Application Number Title Priority Date Filing Date
US483395A Expired - Lifetime US3454362A (en) 1965-03-16 1965-08-26 Process for producing fibrous graphite
US787356A Expired - Lifetime US3503708A (en) 1965-03-16 1968-12-27 Graphite yarn

Family Applications After (1)

Application Number Title Priority Date Filing Date
US787356A Expired - Lifetime US3503708A (en) 1965-03-16 1968-12-27 Graphite yarn

Country Status (2)

Country Link
US (2) US3454362A (en)
GB (1) GB1093084A (en)

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3634035A (en) * 1969-04-28 1972-01-11 Celanese Corp Continuous production of uniform graphite fibers
US3652221A (en) * 1969-07-30 1972-03-28 Union Carbide Corp Process for producing carbon fibers
US3663173A (en) * 1968-05-31 1972-05-16 Stevens & Co Inc J P Process for producing carbonized fibrous products
US3716331A (en) * 1970-04-10 1973-02-13 Union Carbide Corp Process for producing carbon fibers having a high young's modulus of elasticity
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
US4671950A (en) * 1984-11-14 1987-06-09 Toho Beslon Co., Ltd. High-strength carbonaceous fiber
US4765458A (en) * 1986-10-14 1988-08-23 Ni Industries, Inc. Asbestos free hardened monolithic filler mass
US4915926A (en) * 1988-02-22 1990-04-10 E. I. Dupont De Nemours And Company Balanced ultra-high modulus and high tensile strength carbon fibers
EP0374925A2 (en) * 1988-12-22 1990-06-27 Toho Rayon Co., Ltd. High density graphite fiber and method of manufacture thereof
US5169718A (en) * 1989-06-22 1992-12-08 Toyota Jidosha Kabushiki Kaisha Sliding member
US5202293A (en) * 1989-01-17 1993-04-13 Toyota Jidosha Kabushiki Kaisha Carbon fiber reinforced carbon
US5632788A (en) * 1995-01-31 1997-05-27 Worthington Acetylene Cylinder, Inc. High porosity calcium silicate mass for storing acetylene gas
US20080090035A1 (en) * 2006-07-26 2008-04-17 Emmanuel Baune Gas container packing structure having a material crystallized in needle form
US7807259B2 (en) 2006-07-26 2010-10-05 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Gas vessel packing structure having a crystalline phase
WO2011015751A1 (en) 2009-08-05 2011-02-10 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Porous ceramic material having a macroporosity controlled by layering pore-forming agents
WO2011015750A1 (en) 2009-08-05 2011-02-10 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Porous ceramic material having a cellular structure and a controlled macroporosity
US20110108514A1 (en) * 2008-07-02 2011-05-12 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for Producing a Packing Structure with Control Over the Drying Step
US20110207596A1 (en) * 2008-07-02 2011-08-25 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for Producing a Packing Structure with Control Over Hydrothermal Synthesis Parameters
EP2540684A1 (en) 2011-06-30 2013-01-02 L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Porous silica and portlandite material for lining insulation bricks with controlled structure and associated manufacturing method

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4284612A (en) * 1980-01-28 1981-08-18 Great Lakes Carbon Corporation Preparation of SiC whiskers
US4351816A (en) * 1980-12-17 1982-09-28 Union Carbide Corporation Method for producing a mesophase pitch derived carbon yarn and fiber
US4371129A (en) * 1980-12-17 1983-02-01 Union Carbide Corporation Bobbin for use in producing a mesophase pitch derived carbon yarn
US4610860A (en) * 1983-10-13 1986-09-09 Hitco Method and system for producing carbon fibers
GB2170491A (en) * 1985-02-04 1986-08-06 Fiber Materials Method of producing graphite fiber and product thereof
JPS63211326A (en) * 1987-02-20 1988-09-02 Toray Ind Inc Graphite fiber having high compression strength
US4979998A (en) * 1989-10-10 1990-12-25 Union Carbide Corporation Process for forming a metal boride coating on a carbonaceous substrate
KR101138291B1 (en) 2009-05-08 2012-04-24 국방과학연구소 Method for manufacturing Lyocell based carbon fiber and Lyocell based carbon fabric
EP3663751A1 (en) * 2018-12-07 2020-06-10 Universität Augsburg Method and apparatus for assessing physical properties of a para- or diamagnetic structure such as a carbon fiber

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2263217A (en) * 1938-06-24 1941-11-18 Owens Corning Fiberglass Corp Heat treatment of glass textiles
US2509292A (en) * 1946-10-17 1950-05-30 Celanese Corp Production of stretched artificial yarns and textile materials made therefrom
US2624934A (en) * 1948-04-23 1953-01-13 W M Steele Company Inc Method of and apparatus for heat treatment of filamentary material
US2957756A (en) * 1958-03-18 1960-10-25 Union Carbide Corp Filamentary graphite and method for producing the same
US3011981A (en) * 1958-04-21 1961-12-05 Soltes William Timot Electrically conducting fibrous carbon
US3107152A (en) * 1960-09-12 1963-10-15 Union Carbide Corp Fibrous graphite
US3116975A (en) * 1961-02-08 1964-01-07 Union Carbide Corp Artificial graphite process
US3179605A (en) * 1962-10-12 1965-04-20 Haveg Industries Inc Manufacture of carbon cloth
US3285696A (en) * 1960-08-25 1966-11-15 Tokai Denkyoku Seizo Kabushiki Method for the preparation of flexible carbon fibre
US3304148A (en) * 1963-06-17 1967-02-14 Haveg Industries Inc Carbon cloth annealing process

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2263217A (en) * 1938-06-24 1941-11-18 Owens Corning Fiberglass Corp Heat treatment of glass textiles
US2509292A (en) * 1946-10-17 1950-05-30 Celanese Corp Production of stretched artificial yarns and textile materials made therefrom
US2624934A (en) * 1948-04-23 1953-01-13 W M Steele Company Inc Method of and apparatus for heat treatment of filamentary material
US2957756A (en) * 1958-03-18 1960-10-25 Union Carbide Corp Filamentary graphite and method for producing the same
US3011981A (en) * 1958-04-21 1961-12-05 Soltes William Timot Electrically conducting fibrous carbon
US3285696A (en) * 1960-08-25 1966-11-15 Tokai Denkyoku Seizo Kabushiki Method for the preparation of flexible carbon fibre
US3107152A (en) * 1960-09-12 1963-10-15 Union Carbide Corp Fibrous graphite
US3116975A (en) * 1961-02-08 1964-01-07 Union Carbide Corp Artificial graphite process
US3179605A (en) * 1962-10-12 1965-04-20 Haveg Industries Inc Manufacture of carbon cloth
US3304148A (en) * 1963-06-17 1967-02-14 Haveg Industries Inc Carbon cloth annealing process

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3663173A (en) * 1968-05-31 1972-05-16 Stevens & Co Inc J P Process for producing carbonized fibrous products
US3634035A (en) * 1969-04-28 1972-01-11 Celanese Corp Continuous production of uniform graphite fibers
US3652221A (en) * 1969-07-30 1972-03-28 Union Carbide Corp Process for producing carbon fibers
US3716331A (en) * 1970-04-10 1973-02-13 Union Carbide Corp Process for producing carbon fibers having a high young's modulus of elasticity
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
US4671950A (en) * 1984-11-14 1987-06-09 Toho Beslon Co., Ltd. High-strength carbonaceous fiber
US4765458A (en) * 1986-10-14 1988-08-23 Ni Industries, Inc. Asbestos free hardened monolithic filler mass
US4915926A (en) * 1988-02-22 1990-04-10 E. I. Dupont De Nemours And Company Balanced ultra-high modulus and high tensile strength carbon fibers
EP0374925A2 (en) * 1988-12-22 1990-06-27 Toho Rayon Co., Ltd. High density graphite fiber and method of manufacture thereof
EP0374925A3 (en) * 1988-12-22 1991-09-25 Toho Rayon Co., Ltd. High density graphite fiber and method of manufacture thereof
US5202293A (en) * 1989-01-17 1993-04-13 Toyota Jidosha Kabushiki Kaisha Carbon fiber reinforced carbon
US5169718A (en) * 1989-06-22 1992-12-08 Toyota Jidosha Kabushiki Kaisha Sliding member
US5632788A (en) * 1995-01-31 1997-05-27 Worthington Acetylene Cylinder, Inc. High porosity calcium silicate mass for storing acetylene gas
US20110100843A1 (en) * 2006-07-26 2011-05-05 L'air Liquide, Societe Anonyme Pour I'etude Et I'exploitation Des Procedes Georges Claude Gas vessel packing structure having a crystalline phase
US7807259B2 (en) 2006-07-26 2010-10-05 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Gas vessel packing structure having a crystalline phase
US20080090035A1 (en) * 2006-07-26 2008-04-17 Emmanuel Baune Gas container packing structure having a material crystallized in needle form
US7972667B2 (en) 2006-07-26 2011-07-05 L'Air Liquide Societe Anonyme pour l'Etude et l'Exploitation des Procedes G eorges Claude Gas container packing structure having a material crystallized in needle form
US8241715B2 (en) 2006-07-26 2012-08-14 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Gas vessel packing structure having a crystalline phase
US20110108514A1 (en) * 2008-07-02 2011-05-12 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for Producing a Packing Structure with Control Over the Drying Step
US20110207596A1 (en) * 2008-07-02 2011-08-25 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for Producing a Packing Structure with Control Over Hydrothermal Synthesis Parameters
US8628708B2 (en) 2008-07-02 2014-01-14 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for producing a packing structure with control over the drying step
WO2011015751A1 (en) 2009-08-05 2011-02-10 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Porous ceramic material having a macroporosity controlled by layering pore-forming agents
WO2011015750A1 (en) 2009-08-05 2011-02-10 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Porous ceramic material having a cellular structure and a controlled macroporosity
EP2540684A1 (en) 2011-06-30 2013-01-02 L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Porous silica and portlandite material for lining insulation bricks with controlled structure and associated manufacturing method
WO2013000859A1 (en) 2011-06-30 2013-01-03 L'air Liquide,Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Porous material containing silica and portlandite for filling insulation bricks having a controlled structure, and related production method

Also Published As

Publication number Publication date
US3503708A (en) 1970-03-31
GB1093084A (en) 1967-11-29

Similar Documents

Publication Publication Date Title
US3454362A (en) Process for producing fibrous graphite
EP2233616B1 (en) Processes for producing flameproof fiber and carbon fiber
Diefendorf et al. High‐performance carbon fibers
Watt Production and properties of high modulus carbon fibres
Jones et al. Structural development in mesophase pitch based carbon fibers produced from naphthalene
Damodaran et al. Chemical and physical aspects of the formation of carbon fibres from PAN-based precursors
US3533743A (en) Process for the manufacture of continuous high modulus carbon yarns and monofilaments
Trinquecoste et al. High temperature thermal and mechanical properties of high tensile carbon single filaments
US3818082A (en) Process for the production of carbonaceous tapes
US3528774A (en) Formation of high modulus,high strength graphite yarns
WO1991006695A1 (en) Linear carbonaceous fiber with improved elongatability
US3671192A (en) Method of stabilizing acrylic polymer fibers prior to graphitization
US3716331A (en) Process for producing carbon fibers having a high young's modulus of elasticity
US3705236A (en) Method of producing carbon fibers
Ezekiel et al. Preparation of graphite fibers from polymeric fibers
EP0280233B1 (en) Method for producing carbon-carbon composite materials
US3652221A (en) Process for producing carbon fibers
US5695816A (en) Process for the preparation of carbon fiber reinforced carbon composites
McHenry et al. Elevated temperature strength of silicon carbide-on-carbon filaments
Economy et al. Carbonisation and hot stretching of a phenolic fibre
US3533741A (en) Process for the production of filamentary carbon
KR100918686B1 (en) The method for manufacturing the spun-type carbon fiber fabrics from spun-type stabilized polyacrylonitirle fibers
EP0242401B1 (en) Process for producing carbon fibers
US3556712A (en) Method of making flame-proof fibers
US3816598A (en) Process for surface treatment of graphite fibers

Legal Events

Date Code Title Description
AS Assignment

Owner name: AMOCO CORPORATION, A CORP. OF INDIANA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:UNION CARBIDE CORPORATION;REEL/FRAME:004634/0001

Effective date: 19860620