EP0014161B1

EP0014161B1 - Method of treating a multifilament bundle of pitch fibers and a spin size composition therefor

Info

Publication number: EP0014161B1
Application number: EP19800400136
Authority: EP
Inventors: John Baldwin Barr; Nicholas Francis White Iii
Original assignee: Union Carbide Corp
Current assignee: Union Carbide Corp
Priority date: 1979-01-29
Filing date: 1980-01-28
Publication date: 1983-03-30
Also published as: DE3062488D1; EP0014161A2; EP0014161A3

Description

Background of the invention

This invention relates to a spin size and thermosetting aid for pitch fibers.
In order to convert pitch fibers into carbon fibers it is necessary to first thermoset them before they can be carbonized to produce the desired final product. Generally, such fibers are spun and further processed into carbon in the form of multifilament yarn or tow. Because of the exothermic nature of pitch oxidation, however, hot spots often develop in the multifilament bundle during thermosetting which cause the fibers to melt or soften before they become infusibilized. As a result of this, deformation of the individual filaments occurs along with exudation of molten pitch through the filament surfaces which causes them to stick together at various points of contact along the length of the yarn or tow. This deformation and sticking of the fibers in turn causes the yarn or tow to become stiff and brittle and to suffer a loss of flexibility and tensile strength. As a result, such yarn or tow cannot be further processed without breaking a large number of filaments.
Spin sizes are conveniently applied to pitch fiber yarn or tow immediately following spinning in order to maintain the integrity of the yarn or tow, to provide lubricity at the filament-to- filament interfaces, and to impart abrasion resistance to the filament bundle. However, while such sizes improve the handleability of the yarn or tow prior to thermosetting, they often are of no value, or only of limited value, during thermosetting. Thus, for example, while mixtures of plain water and glycerol impart good handling properties to as-spun pitch fiber yarn or tow, such yarn or tow is still subject to the same disadvantages encountered during thermosetting of unsized yarn or tow, i.e., melting and sticking of the fibers often occurs which causes a reduction of the flexibility and tensile strength of the fiber bundle.
One attempt to overcome the sticking problem encountered during thermosetting is disclosed in SU-A-1 68,848. The approach to the problem suggested in that reference is to fan the filaments with coal dust prior to thermosetting. However, not only is this method dirty and inconvenient, but it is also very difficult to apply a uniform layer of particles to the filaments by this technique. Furthermore, because coal has a high inorganic impurity content, significant pitting of the fiber surfaces occurs during oxidation which is accompanied by a concomitant reduction in the strength of the fibers after carbonization.
A similar attempt to surmount the sticking problem and at the same time accelerate oxidation of pitch fibers is disclosed in U.S.-A-3,997,645 wherein it is suggested that the fibers be dusted with activated carbon which has been impregnated with an oxidizing agent. However, this procedure appears to suffer from the same disadvantages as the process of SU-A-168,848. Furthermore, because of the hardness and large size of the particles employed (60 µm), this procedure does not provide sufficient separation of the filament bundle to allow maximum contact of the oxidizing gas with the fiber surfaces or provide sufficient lubricity between the fibers to prevent physical damage to the fiber surfaces.

Summary of the invention

The present invention provides a method of treating a multifilament bundle of pitch fibers, such as yarn or tow, to prepare such multifilament bundle for further processing which comprises applying to the fibers thereof an aqueous finishing composition comprising a dispersion of graphite or carbon black in water in which is dissolved a water-soluble oxidizing agent and a water-soluble surfactant.

Description of the preferred embodiments

The aqueous dispersion employed to treat a multifilament bundle of pitch fibers according to the present invention serves as both a size for the bundle and as an effective thermosetting aid during the infusibilization step which must be conducted before the fibers can be carbonized to produce the desired product. Because the graphite or carbon black particles are applied as a finely-divided dispersion, more effective penetration of these particles between the filaments of the bundle is achieved. As a result of this increased penetration of the particles, greater lubricity is provided between the filaments which helps prevent physical damage to the fiber surfaces during subsequent processing. In addition, the separation of the fiber bundle caused by the infiltration of these minute particles between the filaments allows improved penetration of the oxidizing gas into the bundle during thermosetting, which helps reduce oxidation time and the exothermic excursion and filament fusion which ordinarily occurs at that time. As noted previously, such fusion reduces the flexibility and tensile strength of the yarn or tow.
Either finely-divided graphite or carbon black can be employed in the dispersions employed in the present invention.
Materials such as activated carbon and coal are undesirable because they are abrasive and contain a high amount of inorganic impurities (usually several percent) which is known to cause pitting of the fiber surfaces during oxidation and a concomitant loss of fiber strength. For this reason, it is preferable to use graphite or carbon black as they are softer, more slippery materials and are available in a relatively pure state compared to other carbonaceous materials. For best results, the graphite or carbon black should contain less than 0.5 percent by weight of inorganic impurities. This inorganic impurity content is usually measured by determining the ash content of such materials.
Any form of carbon black, e.g. gas blacks, furnace combustion blacks, furnace thermal blacks, lampblacks, may be employed in the dispersions of the present invention. Likewise, any form of graphite, either natural or synthetic, can be employed. In order to allow maximum penetration of such particles between the filaments of the fiber bundle, they should be no greater than 15 pm in size. Preferably, they have a size of from 0.3 pm to 5,um. Because of the small size of these particles they readily infiltrate the fiber bundle and uniformly coat the filaments. When the fiber bundle is further processed, these soft and slippery particles readily slide over each other and over the filaments so that the fibers are less subject to breakage and damage. Furthermore, the separation of the fiber bundle caused by the infiltration of these minute particles between the filaments facilitates permeation of the oxidizing gas into the bundle during thermosetting. This increased permeation of oxygen into the fiber bundle reduces the oxidation time and allows the fibers to be processed at greatly increased speeds. Ordinarily, unless filament packing in the fiber bundle is kept low and the oxidation process is very gradual, an exotherm excursion occurs during oxidation which causes fusion of the filaments to occur. Because of the separation of the fiber bundle caused by the infiltration of the graphite or carbon black particles between the filaments, however, the filament surfaces are brought into contact with the oxidizing gas to a greater content during oxidation and such heat excursion is prevented. As a result, the fibers can be more rapidly oxidized without the fusion and filament sticking which formerly occurred. Thus, throughout speeds of at least 1.5 times that formerly attained without the use of such dispersions are now possible without loss of fiber properties. As a result, production capacity and the economics of the process have been greatly improved.
By adjusting the concentration and wetting characteristics of the dispersion employed in the present invention, it is possible to control the amount of graphite or carbon black which is deposited on the pitch fiber bundle. Generally, the dispersion contains from about 0.1 part by weight to about 10 parts by weight of graphite or carbon black per 100 parts by weight of mixture, preferably from 1 part by weight to 6 parts by weight of graphite or carbon black per 100 parts by weight of mixture.
Any water-soluble compound which is capable of functioning as an oxidizing agent at the temperature at which thermosetting is effected can be employed as a thermosetting aid in the aqueous dispersions employed in the present invention, provided such compound does not cause the suspension to flocculate. Because the compounds employed are water soluble, their physical presence on the fiber surfaces during thermosetting is assured. Oxidation and infusibilization of the fibers is thereby enhanced during thermosetting, allowing the fibers to be processed at greatly increased speeds. Suitable oxidizing agents include peroxygenated compounds, for example, peroxides, persulfates, pyrosulfates, and perchlorates. Among the compounds which can be employed are sodium peroxide, potassium peroxide, sodium persulfate, potassium persulfate, sodium pyrosulfate, potassium pyrosulfate, sodium perchlorate, potassium perchlorate, and magnesium perchlorate. Sulfates, sulfites, bisulfites, sulfamates, and nitrates are also suitable, including, for example, sodium sulfate, potassium sulfate, sodium sulfite, potassium sulfite, sodium bisulfite, potassium bisulfite, sodium sulfamate, potassium sulfamate, sodium nitrate, and potassium nitrate. However, because such salts leave residues on the fibers and may cause pitting of the fiber surfaces during oxidation, it is preferred to use the corresponding ammonium salts or such compounds as hydrogen peroxide and sulfamic acid.
Any water soluble surfactant can be employed in the aqueous dispersions employed in the present invention, provided such surfactant does not cause the suspension to flocculate. Anionic and nonionic surfactants are preferred for this reason. Such surfactants serve to increase wetting of the fibers by the dispersion by reducing the surface tension of the water, thereby promoting the distribution of the graphite or carbon black throughout the fiber bundle. As a result, oxidation and infusibilization of the fibers during thermosetting is enhanced and the fibers can be processed at greatly increased speeds. Suitable surfactants include tetramethyl sodium oleate, tetramethyl sodium laurate, sodium laurate, and the like. However, because such salts leave residues on the fibers and may cause pitting of the fiber surfaces during oxidation, it is preferred to use the corresponding ammonium salts.
Generally, an amount. of surfactant is employed which will impart a surface tension of less than about 0.05 N/m to the dispersion, preferably less than about 0.04 N/m. The amount of oxidizing agent employed should not exceed an amount of which will destroy the stability of such dispersion. Generally, from about 0.1 part by weight to about 2.0 parts by weight, preferably from about 0.2 part by weight to about 0.8 part by weight, per 100 parts by weight of mixture are satisfactory. If necessary, a suitable dispersing agent may be employed to facilitate dispersion of the graphite or carbon black in the water and maintenance of the dispersion. Suitable stabilizers, film formers, etc. may also be employed if desired.
A water-soluble surfactant which is also capable of functioning as an oxidizing agent at the temperature at which thermosetting is effected can be employed in the aqueous dispersions employed in the present invention, provided such oxidation agent-surfactant does not cause the suspension to flocculate. Anionic surfactants are preferred for this reason. Such oxidizing agent-surfactants serve both to increase wetting of the fibers by the dispersion and as a thermosetting aid during the subsequent infusibilization step. By reducing the surface tension of the water they promote the distribution of the graphite or carbon black throughout the fiber bundle and their own presence on the fiber surfaces, thereby further enhancing the oxidation and infusibilization of the fibers during thermosetting and allowing them to be processed at greatly increased speeds. Suitable oxidizing agent-surfactants include alkali metal hydrocarbyl sulfates, for example, alkali metal aryl sulfates and alkali metal alkyl sulfates. Among the compounds which can be employed are sodium 2-ethylhexyl sulfate, sodium heptadecyl sulfate, and sodium tetradecyl sulfate. These compounds are sold commercially under the trademark "Tergitol"^*. However, because such salts leave residues on the fibers and may cause pitting of the fiber surfaces during oxidation, it is preferred to use the corresponding ammonium salts.
^*"Tergitol" is a registered trademark of Union Carbide Corporation.
Generally, from about 0.2 part by weight to about 20 parts by weight, preferably from about 0.6 part by weight to about 4 parts by weight, of the oxidizing agent/surfactant per 100 parts by weight of mixture can be employed in the dispersion. If necessary, a suitable dispersing agent may be employed to facilitate dispersion of the graphite or carbon black in the water and maintenance of the dispersion. Likewise, oxidizing agents and wetting agents over and above the oxidizing agent/surfactant employed may be added to the dispersion to facilitate oxidation or wetting of the fibers, although they are unnecessary. Suitable stabilizers, film formers, etc. may also be employed if desired.
After the dispersion has been formed, it is applied to the fibers by any convenient means, such as by spraying, brushing, rolling, or simply by immersing the fibers in the dispersion. A convenient means of applying the dispersion to the fibers is to pass the fibers over a sizing wheel which rotates in a bath of the dispersion and is coated with the dispersion. This, preferably, is done as the fibers emerge from the spinnerette. By controlling the size and speed of the wheel it is possible to control the amount of the dispersion which is applied to the fibers. In any event, the fibers should be allowed to absorb a sufficient amount of the suspension to providefrom about 0.1 gram of the dispersion to about 1.5 grams of the dispersion per gram of fiber.
The fibers treated in this manner are then thermoset in a conventional manner by heating in an oxygen-containing atmosphere, such as pure oxygen or air. Drying of the fibers is not necessary and the fibers can be thermoset while still wet if desired. Such thermosetting, of course, must be carried out at a temperature below the temperature at which the fibers soften or distort. Because the thermosetting action of the oxidizing agent employed usually commences at a temperature below 200°C where the rate of oxidation is ordinarily quite slow, infusibilization can usually be effected at lower temperatures than are normally required, or in shorter periods of time than are normally required. While the time required to oxidize the fibers to the desired degree will vary with such factors as the particular oxidizing atmosphere, the temperature employed, the diameter of the fibers, and the particular pitch from which the fibers were prepared, at any given temperature such time is usually less than two-thirds of the time required when the fibers are not treated with the dispersions of the present invention.
The thermoset fibers may then be carbonized in a conventional manner by heating them in an inert atmosphere to a temperature sufficiently elevated to remove hydrogen and other carbonizable by-products and produce a substantially all-carbon fiber. Fibers having a carbon content greater than about 98 percent by weight can generally be produced by heating to a temperature in excess of about 1000°C, and at temperatures in excess of about 1500°C the fibers are completely carbonized. Generally, carbonization times of from about 2 seconds to about 1 minute are sufficient.
If desired, the carbonized fibers may be further heated in an inert atmosphere to a graphitization temperature, e.g. from about 2500°C to about 3300°C.
Pitch fibers suitable for use in the present invention can be prepared in accordance with well-known techniques. Preferably, the fibers employed are prepared from mesophase pitch as described in U.S.-A-4,005,183.
While the invention has been described with reference to pitch fiber yarn or tow, it should be apparent that fibers or other carbonizable organic polymeric materials, such as homopolymers and interpolymers or acrylonitrile, can be treated in a similar manner.
The following examples are set forth for purposes of illustration so that those skilled in the art may better understand this invention. It should be understood, however, that they are exemplary only, and should not be construed as limiting this invention in any manner. Tensile strength and pull strength properties referred to in the examples and throughout the specification were determined as described below unless otherwise specified.

Tensile strength

Tensile strength was determined on an "Instron" (Registered Trade Mark) testing machine at a cross-head speed of 0.02 cm/min. All measurements were made on 254 mm length unidirectional fiber-epoxy composites.

Pull strength

Pull strength was determined on Mechanical Force Gage Model D-20-T, manufactured by Hunter Spring Co., Hatfield, Pa., a division of Ametak Inc. The filament or filament bundle to be tested is passed over a pulley which is attached by means of a spring to a gauge designed to record the force in pounds exerted on the pulley. Both ends of the filament or filament bundle are then wrapped around a mandrel which is suspended from the pulley by means of the filament or filament bundle. Typically, a distance of from about 76.2 to 304.8 mm is provided between the pulley and the mandrel. Tension is then exerted on the filament or filament bundle by pulling down on the mandrel until the yarn breaks. The total force in pounds required to break the filament or filament bundle is recorded on the gauge. This force is designated as the pull strength of the filament or filament bundle.

Example 1

Continuous pitch filaments were spun through two 1000 hole hot melt spinnerettes from a 322°C softening point mesophase pitch having a mesophase content of 77 percent. The capillary holes of the spinnerette were 0.10 mm in diameter and 0.20 mm in length. As the filaments emerged from the spinnerette, they were combined into a single bundle which was drawn down over a sizing wheel which rotated in a bath containing a suspension of carbon black flour in an aqueous solution of ammonium persulfate and ammonium laurate. The fibers were spread over the slowly rotating wheel as they were brought into contact with it and were thoroughly wetted by and uniformly coated with the suspension by this procedure. The coated fibers were then collimated into a yarn by means of a gathering wheel having a "V" slot, and subsequently drawn down to a diameter of about 14 microns by means of two godet wheels.
The suspension employed to coat the fibers contained 3.6 parts by weight of carbon black, 0.8 part by weight of ammonium persulfate, and 0.4 part by weight of ammonium laurate per 100 parts by weight of mixture. The carbon black particles present in the suspension had an average size of 0.5 micron. The composition was prepared by admixing (a) 3.2 parts by weight of an aqueous solution containing 25 parts by weight of ammonium persulfate in 75 parts by weight of water with (b) 20 parts by weight of an aqueous solution containing 2 parts by weight of ammonium laurate in 98 parts by weight of water, and (c) 6.4 parts by weight of "Dylon"^* DS insulating carbon coating (a commercially available suspension of 56 parts by weight of amorphous carbon in 44 parts by weight of water), and then adjusting the pH of the mixture to 10 by means of ammonium hydroxide to give 100 parts of mixture.
The fibers treated in this manner were then thermoset by transporting them through a 12.2 m long forced air convection furnace at a speed of 152 mm per minute. The furnace contained eight zones, each 1.52 m in length, and the fibers were gradually heated from 175°C in the first or entrance zone to 380°C in the eighth or exit zone while air was passed through the furnace at a velocity of 1.22 m/minute. Total residence time in the furnace was 80 minutes. The fibers produced in this manner were totally infusible. A 76.2 mm length of the thermoset fibers had a pull strength of 22.7 N (5.1 lbs) and a 304.8 mm length had a pull strength of 13.8 N (3.1 Ibs). (By 76.2 mm and 304.8 mm lengths is meant the distance between the pulley and the mandrel of the Mechanical Force Gage employed in the determination).
The thermoset fibers were then wound on a roller and carbonized by heating them in a nitrogen atmosphere at a temperature of about 2200°C for 3 seconds. After carbonization, the fibers had a strand tensile strength of 20.8 x 10⁸ Pa.

Example 2

The procedure of Example 1 was repeated employing a colloidal suspension of graphite flour in an aqueous solution of ammonium persulfate and ammonium laurate. The suspension contained 3.6 parts by weight of graphite, 0.8 part by weight of ammonium persulfate, and 0.4 part by weight of ammonium laurate per 100 parts by weight of mixture. The graphite particles present had an average size of 1 micron. This composition was prepared by admixing (a) 3.2 parts by weight of an aqueous solution containing 25 parts by weight of ammonium persulfate in 75 parts by weight of water with (b) 20 parts by weight of an aqueous solution containing 2 parts by weight of ammonium laurate in 98 parts by weight of water, and (c) 16.4 parts by weight of "Aquadag"^* micro-graphite colloid in aqueous suspension (a commercially available colloidal suspension of 22 parts by weight of graphite in 78 parts by weight of water), and then adjusting the pH of the mixture to 9.7 by means of ammonium hydroxide to give 100 parts of mixture.
After thermosetting, a 76.2 mm length of the fibers had a pull strength of 20.9 N (4.7 lbs) and

^*"Dylon" is a Registered Trade Mark of Dylon Industries.
^*"Aquadag" is a Registered Trade Mark of Acheson Colloids Company.

When the procedure was repeated eliminating the ammonium persulfate from the colloidal suspension employed to treat the fibers, a 76.2 mm length of the thermoset fibers had a pull strength of 10.7 N (2.4 lbs) and a 304.8 mm length had a pull strength of 8.0 N (1.8. lbs).

Example 3

Continuous pitch filaments were spun through two 1000 hole hot melt spinnerettes from a 322°C softening point mesophase pitch having a mesophase content of 77 percent. The capillary holes of the spinnerette were 0.10 mm in diameter and 0.20 mm in length. As the filaments emerged from the spinnerette, they were combined into a single bundle which was drawn down over a sizing wheel which rotated in a bath containing a colloidal suspension of graphite flour in an aqueous solution of ammonium 2-ethylhexyl sulfate. The fibers were spread over the slowly rotating wheel as they were brought into contact with it and were thoroughly wetted by and uniformly coated with the suspension by this procedure. The coated fibers were then collimated into a yarn by means of a gathering wheel having a "V" slot, and subsequently drawn down to a diameter of about 14 microns by means of two godet wheels.
The colloidal suspension employed to coat the fibers contained 3.6 parts by weight of graphite and 2.7 parts by weight of ammonium 2-ethylhexyl sulfate per 100 parts by weight of mixture. The graphite particles present had an average size of 1 micron. This composition was prepared by admixing 8.7 parts by weight of an aqueous solution containing 31 parts by weight of ammonium 2-ethylhexyl sulfate in 69 parts by weight of water with 16.4 parts by weight of "Aquadag"^* micro-graphite colloid in aqueous suspension (a commercially available colloidal suspension of 22 parts by weight of graphite in 78 parts by weight of water), and then adjusting the pH of the mixture to 10 by means of ammonium hydroxide to give 100 parts of mixture.
The fibers treated in this manner were then thermoset by transporting them through a 12.2 m long forced air convection furnace at a speed of 152 mm per minute. The oven contained eight zones, each 1.52 m in length, and the fibers were gradually heated from 175°C in the first or entrance zone to 380°C in the eighth or exit zone while air was passed through the furnace at a velocity of 1.22 m/minute. Total residence time in the furnace was 80 minutes. The fibers produced in this manner were totally infusible. A 76.2 mm length of the thermoset fibers had a pull strength of 21.8 N (4.9 lbs) and 304.8 mm length had a pull strength of 20.5 N

^*"Aquadag" is a Registered Trade Mark of Acheson Colloids Company.

The thermoset fibers were then wound on a roller and carbonized by heating them in a nitrogen atmosphere at a temperature of about 2200°C for 3 seconds. After carbonization, the fibers had a strand tensile strength of 17.0 x 10⁸ Pa.
When the procedure was repeated substituting a like amount of sodium 2-ethylhexyl sulfate for ammonium 2-ethylhexyl sulfate in the colloidal suspension employed to treat the fibers, a 304.8 mm length of the thermoset fibers had a pull strength of 18.3 N (4.1 lbs). The carbonized fibers had a strand tensile strength of 13.3×10⁸ Pa.
When the procedure was again repeated substituting 0.4 part by weight of ammonium laurate for ammonium 2-ethylhexyl sulfate in the colloidal suspension employed to treat the fibers, a 76.2 mm length of the thermoset fibers had a pull strength of 10.7 N (2.4 lbs) and a 304.8 mm length had a pull strength of 8.0 N (1.8 lbs). These fibers were stiff, brittle, and too fused and weak to be wound on a roller and carbonized.
When the fibers were treated in like manner with suspensions containing from 1 part by weight to 3 parts by weight of colloidal graphite and from 0.08 part by weight to 0.39 part by weight of tetramethyl ammonium oleate per 100 parts by weight of mixture, 304.8 mm lengths of the thermoset fibers had pull strengths of from 1.3 N (0.3 lb) to 11.6 N (2.6 lbs). These fibers were stiff, brittle, and too fused and weak to be wound on a roller and carbonized.

Example 4

The procedure of Example 3 was repeated employing a suspension of carbon black flour in an aqueous solution of sodium 2-ethylhexyl sulfate. The suspension contained 3.6 parts by weight of carbon black and 2.7 parts by weight of sodium 2-ethylhexyl sulfate per 100 parts by weight of mixture. The carbon black particles present in the suspension had an average size of 0.5 micron. The composition was prepared by admixing 6.8 parts by weight of an aqueous solution containing 40 parts by weight of sodium 2-ethylhexyl sulfate in 60 parts by weight of water with 6.4 parts by weight of "Dylon"^* DS insulating carbon coating (a commercially available suspension of 56 parts by weight of amorphous carbon in 44 parts by weight of water), and then adjusting the pH of the mixture to 10 by means of ammonium hydroxide to give 100 parts of mixture.
After thermosetting, a 304.8 mm length of fibers had a pull strength of 33.4 N (7.5 lbs).

^*"Dylon" is a Registered Trade Mark of Dylon Industries.

When the procedure was repeated eliminating the sodium 2-ethylhexyl sulfate from the suspension employed to treat the fibers, 304.8 mm lengths of the thermoset fibers had a pull strength of 3.6 N (0.8 Ib). These fibers were stiff, brittle, and too fused and weak to be wound on a roller and carbonized.
When the procedure was again repeated substituting a like amount of ammonium 2-ethylhexyl sulfate for sodium 2-ethylhexyl sulfate in the suspension employed to treat the fibers, a 76.2 mm length of the thermoset fibers had a pull strength of 24.0 N (5.4 lbs) and a 304.8 mm length had a pull strength of 13.8 N (3.1 lbs). The carbonized fibers had a strand tensile strength of 20.5x 1 0⁸ Pa.
When 0.4 parts by weight of ammonium laurate was substituted for sodium 2-ethylhexyl sulfate in the suspension, a 76.2 mm length of the thermoset fibers had a pull strength of 7.6 N (1.7 lbs) and a 304.8 mm length had a pull strength of 7.1 N (1.6 lbs). These fibers were stiff, brittle, and too fused and weak to be wound on a roller and carbonized.
When 0.02 part by weight and 0.07 part by weight of tetramethyl ammonium oleate was substituted for sodium 2-ethylhexyl sulfate in the suspension, 304.8 mm lengths of the thermoset fibers had pull strengths of 2.7 N (0.6 Ib) and 4.9 N (1.1 lbs), respectively. Once again, the fibers were stiff, brittle, and too fused and weak to be wound on a roller and carbonized.

Claims

1. A method of treating a multifilament bundle of pitch fibers to prepare such bundle for further processing which comprises applying to the fibers thereof an aqueous finishing composition comprising a dispersion of finely-divided graphite or carbon black particles in water in which is dissolved a water-soluble oxidizing agent and a water-soluble surfactant.

2. A method as in claim 1, wherein the water-soluble oxidizing agent is a peroxygenated compound.

3. A method as in claim 2, wherein the peroxygenated compound is a persulfate.

4. A method as in claim 1, wherein the water-soluble oxidizing agent is selected from sodium peroxide, potassium peroxide, ammonium peroxide, sodium persulfate, potassium persulfate, ammonium persulfate, sodium pyrosulfate, potassium pyrosulfate, ammonium pyrosulfate, sodium perchlorate, potassium perchlorate, ammonium perchlorate, magnesium perchlorate, sodium sulfate, potassium sulfate, ammonium sulfate, sodium sulfite, potassium sulfite, ammonium sulfite, sodium bisulfite, potassium bisulfite, ammonium bisulfite, sodium sulfamate, potassium sulfamate, ammonium sulfamate, sodium nitrate, potassium nitrate, ammonium nitrate, hydrogen peroxide and sulfamic acid.

5. A method as in claim 1, 2, 3 or 4, wherein the water-soluble surfactant is an anionic or nonionic surfactant.

6. A method as in claim 5, wherein the water-soluble anionic or nonionic surfactant is selected from tetramethyl sodium oleate, tetramethyl ammonium oleate, tetramethyl sodium laurate, tetramethyl ammonium laurate, sodium laurate and ammonium laurate.

7. A method as in claim 1, wherein the water-soluble oxidizing agent is ammonium persulfate and the water-soluble surfactant is ammonium laurate.

8. A finishing composition for a multifilament bundle of pitch fibers comprising a dispersion of finely-divided graphite or carbon black particles in water in which is dissolved a water-soluble oxidizing agent and a water-soluble surfactant.

9. A method of treating a multifilament bundle of pitch fibers to prepare such bundle for further processing which comprises applying to the fibers thereof an aqueous finishing composition comprising a dispersion of finely-divided graphite or carbon black particles in water in which is dissolved a water-soluble surfactant which is also capable of functioning as an oxidizing agent.

10. A method as in claim 1 or 9, wherein the graphite or carbon black particles are no greater than 15 pm in size.

11. A method as in claim 1 or 9, wherein the graphite or carbon black particles are from 0.3 µm to 5 µm in size.

12. A method as in claim 1, 9, 10 or 11, wherein the graphite or carbon black contains less than 0.5 percent by weight of inorganic impurities.

13. A method as in claim 9, wherein the water-soluble surfactant is an anionic surfactant.

14. A method as in claim 13, wherein the anionic surfactant is an alkali metal hydrocarbyl sulfate or an ammonium hydrocarbyl sulfate.

15. A method as in claim 14, wherein the anionic surfactant is selected from sodium 2-ethylhexyl sulfate, sodium heptadecyl sulfate, sodium tetradecyl sulfate, ammonium 2-ethylhexyl sulfate, ammonium heptadecyl sulfate, and ammonium tetradecyl sulfate.

16. A method as in claim 9, 13, 14 or 15, wherein the pitch fibers are prepared from mesophase pitch.

17. A finishing composition for a multifilament bundle of pitch fibers comprising a dispersion of finely divided graphite or carbon black particles in water in which is dissolved a water-soluble surfactant which is also capable of functioning as an oxidizing agent.

18. A finishing composition as in claim 8 or 17, wherein the graphite or carbon black particles are no greater than 15 gm in size.