CARBON FIBERS AND METHODS FOR PRODUCING THE SAME

Abstract: Carbon yarn is produced by spinning continuous pitch yarn, treating the pitch yarn with an oxidizing composition, collecting the pitch yarn into a bulk form, and subjecting the treated pitch yarn to a heat treatment in a substantially non-reactive atmosphere to produce carbon yarn.

Description: CARBON FIBERS AND MRTHODS FOR PRODUCING THE SAME Field of the Invention The invention relates to a mothod for the manufacture of carbon fibers which avoids critical steps previously considered essential manufacturing steps for the production of carbon fibers. More particularly, the invention is directed to a process which eliminates the independent step of infusibilizing a mesophase pitch fiber prior to a earbonizing stop for producing carbon fibers. The invontion also relates to novel carbon fibers and composite materials which include the carbon fiber. Backeround of the Invention Mesophase based carbon fibers are wall known in the art since the issuance of U.s. Patent N0 4,005 183 Numerous patents have issued ralating the manufacture of mesophase pitch suitable for producing carbon fibers. Such patenis include U.S. Patent No. 4,026.788, U.S. Patent No. 3,976,729, and U.S. Patent NO. 4,303,631. It has been found in the art that sesophase pitch suitable for apinning pitch fibers contains at least 40% by weight mesophase so that the mesophase is the continuous phase, and the mesophase pitch upon quiescent heat ins forms domzlns at least 200 microns in size. The spinning of mesophase pitch into continuous pitch fibers for the manufacturing of carbon fibers is usually carried out with a spinning apparatus which spins hundreds of fibers aimultaneoualy. unually from 1500 to 2000 pitch fibers simultansously. The average diameter of the pitch fibers is about 13 microns. The pitch fibers. say 2000, are trasted together in subsequent steps. A bundle of continuous fibers are commonly referred to as "yarn" in tbe art. The carbon fibers are usually produced, packaged for ahipping, and used in composites as yarns. Such yarns are sometimes referred to as "carbon yarns". As used herein, the term "yarn" is z plurality of continuous fibers spun and processed together and the torms "pitch yarn", "infusibilized yarn", "carbon yarn" and "graphite yarn" are used to refer to the yarn at various stages of the manufacturing procass. Generally the method for producing carbon fibers fron mesophase pitch includes the steps of spinning the mesophase pitch into a plurality of pitch fibers (pitch yarn), infusibilizing the pitch fibers (infusibilized pitch yarn), and thereafter subjecting the infusibili:.d pitch fibers to a carbonizing step in n substantially non-reactive atmosphere for producing the carbon fibers (carbon yarn). It is known fros the prior art that the step of infusibilizing the pitch fibers Is essential for the manufacture of carbon fibers because it enables the carbonizing step to be carried out relatively rapidly. The carbonizing step usually requires the yarn to be raised to a temperature of at least about 1000 C. It is desirable to be able to raise the temperature of the yarn fron about toon temperature to the final temperature, for example 1000 C, in a short time without causing deformation of the fibers, fusion between fibers, or s deterioration of the mechanical properties of the carbon yarn. In the prior art, the infusibilizing step is partieularly important for producing mesophase pitch based carbon fibers. Meophase pitch derived carbon fibers are characterized by superior mechanical properties such as tensile stren and Young's modulus because the aromatic molecules of the mesophase pitch tend to orient parallel to the pitch fiber during the spinning of the mesophase pitch fibers. Raising the temperature of mesophase pitch fibers which have not been infusibilized to the softening point of the pitch fibers can result in the disorientation of the armoatic molecules and thereby substantially destroy the possibility of obtaining carbon fibers with superior mechanical properties. The prior art has stressed the necessity of infusibilizing mesophase pitch yarn prior to the carbonizing step in order to avoid an extraordinary long period of tise to raise the temperature of the yarn up from room temperature to the carbonizing temperature without deteriorating the qualities of the carbon yarn to be produced. It is also essential, according to the prior art, to infusibilize non-mesophase pitch fibers to avoid having the fibers soften and thereby result in fusion between fibers in a yarn. The step of infusibilizing pitch yarn is also referred to in the art as r "thermosetting step". The infusibilizing step is an exothermic reaction and the beat generated by the reaction can soften or deforn fibars. The heat can cause fibers in z yarn to adhere or stick to each other and this reduces the tensile strength of the resulting carbon yarn as well as the properties of a composite made with the carbon yarn. This problem has been considered in U.s. Patent No. 4,275,051 and U.S. Patent No. 4,276.278. The manufacturing of carbon fibers as reflected in the patent literature has bean reviewed in the book entitled, "Carbon and Graphite Fibers, Manufacture and Application," published by Noyes Data Corporation, Park Ridge, New Jersey, 1980, edited by marshall Sittig. This hook sets forth the historical development of carbon fibers as derived fros different precursor materials and the techniques patented for their manufacture. In addition, the book describes succinctly the various fiber treatment processes, matrices which are employed with carbon yarn in order to make composites, other reinforced materials which can be included in combination with carbon fibers to make effective composites, and the utilization of the carbon fibers in the manufacture of tertile structures. The International Committee for Characterization and Terminology of Carbon bas published "First Publication of 30 Tentative Definitions@ in Carbon, Vol. 20, pp. 445-449, 1982, to clarify the definition of many terms used in the art. The International Committee bas defined "carbon fiber" as "filaments consisting of Mon-Graphite Carbon obtained by Carbonization either of organic aynthetic or natural fibres (PAN or others) or of fibres drawn from organic precursors such as resins or pitches, and by subsequent heat trestment of the carbonized fibres (up to temperatures of about 3000 K)". The International Comaittes bas also defined "Non-Graphitic Carbon" as bell varieties of substances consisting mainly of the element Carbon with two-dimensional long range order of the carbon atoms in planer bexagonal networks, but without any measurable Crystallographic order in the third direction (c-direction) apart from more or less parallel stacking". The term "graphitic fiber" has been used in the art to describe carbon fibers which have been beat treated to between 2500 and 3000 K The International Committee has pointed out that such fibers in most cases remain non-graphitic carbon so that the common term "graphitic fiber" is incorrect. The International Committee has pointed out, however, that "the tern graphitic carbon is justified if Three Dimensional Crystalline Long Range Order can be detected in the material by diffraction methods, independent of the volute fraction and the homogeneity of distribution of such crystalline domains". According to the prior art, the infusibilizing step is carried out in an oxidizing environment preferably at an elevated temperature in order to increase the rate at which the fibers become infusibilized. U.S. Patent No. 4,389,387 discloses the problems of infusibilizing pitch fibers rapidly and effectively. The patent discloses that it is preferable to combine tens of thousands of pitch fibers into a tow of 10 to JO @@@ in diameter in advance of the treatment for infusibiliring. The pitch fibers are loaded onto s net-belt conveyor and passed through s gaseous mixture of air and a gaseous oxidant such as ozygen. ozone, sulfur dioxide, nitrogen dioxide, etc. with the gasseus oxidant being 0.1 to 10% by volume of the gas mixture. The temperatura for the infusibilizing step in the patent is lower than the softening point of the pitch fibers by at least 5 C to SO'C The time for infusibilizing is disclosed in the patent as from 1 to 4 hours. The patent states that problems of infusibilizing pitch fibars are overcome by sowing the gaseous mixture through the packed pitch fibers. Nevertheless, the patent cautions against too large z packing height of pitch fibers to avoid insufficient removal of the generated heat. South African Patent Application No. 7117853, filed November 4. 1971, entitled "Improvements In Or Relating To The Manufacture Of Carbon Fibers", discloses processes for infusibilizing a fiber after it has been spun and prior to a carbonizing step. The infusibilizing step in the patent is referred to as "stabilizing". That is, "atabilizing" and infusibilizing are the same and are used interchangably in the patent. The precursor materials disclosed in the patent include solutions or extracts of corl, as well as pitches, pitch-like material and tar particularly if they are derived from coal. The South African patent discloses "that spun or eztruded fibre, filament or film consisting of the orgadic material may be stabilized by heat treatment by reacting it with either an aqueous solution of bronine or an aqueous solution of nitric acid containing at least 25%, and preferably at least 40% by weight of XNO3 for at least sufficient time to stabilize the spun or eztruded fibre, filament or fili to heat treatment". The patent further discloses that the stabilized fiber can be further stabilized for a heat treatment by oxidation employing an oxidizing gas, preferably containing molecular oxygen at an elevated temperature. The South African patent discloses that nitric acrid reacts with coal and similar materials decomposing the coal and that the reaction of the nitric acid with the coal is a surface effect, the nitric acid in certain circumstances reacting with the coal violently, or even explosively. According to the South African patent: "If the nitric acid is allowed to react for an excessive period of tine with the spun or extruded fibre, filament or film of the organic material, the nitric acid nay react with the spun or extruded fibre, filament or file of the organic material in ruch a manner as to cause it to decompose. In the case where the organic material is r solution or extract of coal <RTI ID=7.55> as hereinbefore referred to, it is believed the nitric acid map react with the solution or extract of coal, cleaving the large molecules of the solution or extract of coal, thereby causing the solution or extract of coal to bave smaller molecules. This night have the effect of diminishing the strength of s apun or extruded fibre, filament or film of the solutioh or extract of coal or of the carbon fibre, filament or file produced therfrom. Accordingly, the spun or extruded fibre, filament or film, whether of the solution or extract of coal or of other organic material, should not he allowed to react with the aqueous solution of either bromine or nitric acid for such g length of time as will seriously detrimentally affect the properties of the stabilized fibre, filament or film or the carbon fibre, filament or film produced thereform." The South African patent provides z single example for the use of aqueous nitric acid. Example 1 discloses that z single filament having z diameter of 30 microns was cut into lengths and immersed in z solution comprising 50% by weight nitric acid at ambient temperature, about 20 C. The number of cut lengths was not stated in the Patent. The fiber lengths were then washed with water to remove the nitric acid and suspended in z vertical oven which was heated in nitrogen to temperature about 2600C at z heating rate of 300 C per hour and thereafter, the nitrogen atmosphere was replaced by oxygen for five minutes. Subsequently, the fibers were heated in nitrogen at the rate of 30 C per hour to z temperature of 1000 C and this temperature was held for one hour. The remaining two examples of the South African patent disclose the use of brorlne in water instead of aqueous nitric acid. For each of these examples, the rate of temperature increase for the carbonizing step was SOtC per hour to z final temperature of 1000 C. The South African patent discloses that it is imperative that the nitric acid be washed from z fiber in order to avoid z deterioration of the fiber from the nitric acid. The commercial utilization of the disclosure of the South African patent would require a washing step subsequent to a nitric acid treatment and that subsequent to the nitric acid treatment, a heat treatment in oxygen similar to the aforementioned example 1 is necessary. Significantly, each of the examples in the South African patents set forth a carbonizing treatment in which the temperature was increased to 1000 C at a rate of 50 C or 80 C per hour for separate cut lengths of the fiber suspended In a furnace -In contrast, r typically commercial carbonizing step for producing carbon fibers is for s yarn having typically at least 1000 filaments heated to a temperature of about 10000C in r furnace through which yarn passes. The yarn is subjected to a change from room temperature to the carbonizing temperature and again to room temperature. The tine the yarn is subjected to the earbonizing temperature is in the order of about one second or less. Japanese Patent No. 564,,648, based upon Patent Publication Mo. 2510/69, published February 3, 1969, discloses a process of producing carbon fibers from dry distilled petroleum sludhe having a sulfuric acid content below 30'. Spun fibers are given a surface treatment by being exposed to chlorine gas stream at s temperature between room temperature and 60 C or dipped in c hydrogen peroxide, or hydrochloric acid, or nitric acid solution. Subsequently, the fibers are heated to 200 C or more in an oxidizing atmosphere to complete the infusibilizing step. The final step is a heat treatment for carbonizing the treated fibers to produce carbon fibers. The Japanese patent discloses that the surface trestnant is necessary because the direct beating in an oxidizing atmosphere of the spun petroleum sludhe fibers results in the fibers becoming soft and deformed. U.S. Patent No. 3,5959,946 discloses oxidizing treatments for filaments of pitch either continuouzly as the filaments are emerging from the spinning machine or for batches of filaments wound into packages. The hot filaments from the spinning machine are passed through an oxidizing atmosphere ruch as air, ozone, nitric oxide, etc. The patent discloses that the filament from the spinning machine can be cooled to z temperature below its fusion point and then passed through a liquid oxidizing bath such as nitric acid, sulfuric acid, chromic acid, permanganate solutions and the like. The patent discloses that the oxidizing treatments can be applied to batches of filament wound into packages. The patent cautions that "the support of the filament package rust be of such nature and/or construction that it yields or collapses as the wound filament contracts during the oxidation process." the patent further cautions: "The oxidation of filament wound to packages must follow a fairly critical heating regime if the superimposed and adjacent loops of filament are not to fuse together. This regime will naturally vary with the pitch, its previous oxidation history and the type and quality of additive present, if any. The best heating rates and eoaking temperatures for a given material are naturally difficult to determine since the fusion temperature of the pitch changes as the oxidation proceed. Neverthelese, it has been established that a heat treated pitch of the type preferred. as described earlier, will yield filaments that are successfully oxidized by raising the temperature to 100 C in less than 15 minutes, a non-critical step; holding the filament at 100- for about 20 hours; raising the temperatures from 100 to 195 C, at a preferred rate of about 5 C/bour; holding the filament at the later temperature for s period within the range of about 60 to about 120 hours. the upper part of that range being preferred. It should be noted that with certain materials temperature Increase rates of up to 10 C/bour may be tolerated. In any event, the temperature at any time during the oxidation treatment should preferably be not higher than 10 C below the softening point of the pitch at the given tine. This batch type oxidation is best carried out in a circulating oven through which passes a constant flow of air oxygen containing gas. botb fresh and recycled. pre-heated at the desired temperature." such g heating schedule is extremely long in time even after tests have been carried out to optimize tbe process to avoid fusion between filaments. In view of the prior art. it appears that it is essential to carry out a separate infusibilizing step prior to a carbonizing step and that considerable care must be taken for infusibilizing pitch yarn to avoid sticking or fusing of fibers. Many attempts have been made in the ert to simplify and expedite the infusibilizing step. The art, however, does not disclose any process for infusibiliring yarn other than as z separate step. Morecver, the prior art requires an oxidizing atmosphere to infusibil pitch fibers ven after the pitch fiber has been treated with an oxidizing liquid1 such as nitric acid. Summary of the Invention The present invention involves z process for manufactyuring mesophase hased carbon yarn. The process comprises spinning mesophase pitch into z plurality of continuous Fibers, combining the plurality of fibers to form a pitch yarn, contacting the pitch yarn with an oxidizing liquid composition, collecting the pitch yarn into a bulk for and subjecting the pitch yarn in bulk form to c heat treatment in a substantially [inert] non-reactive atmosphere to produce carbon yarn in bulk form. The process can be modified so that the pitch yarn is first collected into z bulk form and thereafter contacted with an oxidizing liquid composition. fbe oxidizing liquid composition enables the infusibiliazing of the pitch yarn in the process according to the invention and also serves as z "size" or "sizing" for the pitch yarn. The teras "wize" and "sizing" are used interchangeably in the art. In this connection1 "mizing" on the pitch yarn tends to maintain the pitch fibers in the pitch yarn together and thereby minimize any separation of pitch fibers from the body of the pitch yarn. It is desirable to maintain the pitch fibers in the pitch yarn close together for the handling of the pitch yarn in the manufacturing operations. Piscussion of the Invantion The invention substantially simplifies the manufacturing of sesophase based carbon yarn and also greatly reduces the cost of manufacturing. This can be better appreciated by comparing the invention with z conventional process of making carbon yarn. Conventional manufacturing of mesophase based carbon yarn utilizes many operations and costly capital equipment. The following is a general description of z conventional manufacturing operation. A spinning apparatus produces 2000 continuous mesophase pitch fibers which are individually drawn down by z drawdown ratio of about S0:l so that the average fiber diameter is about 12 microns. A drawdown is necessary to obtain the small diameter because spinning holes of about 12 microns in diameter would be expensive to produce and would clog easily. It is well known in the art that carbon fibers having small diameters have generally better mechanical properties than relatively large diameter carbon fibers. Small diameter pitch fibers are used to obtain the small diameter carbon fibers. The 2000 pith fibers are sized and gathered together to form r pitch yarn. The infusibilizing step is carried out by leying the pitch yarn onto a conveyor belt in c uniform pattern and the conveyor belt moves the pitch tern Into an oven. The pitch fiber is mtchanically weak and must be manipulated with considerable care. Accordingly, the system for laying the pitch yarn onto the conveyor belt is complex and rate limited. The spinning apparatus is physically located above the conveyor belt. The pitch yarn enters a movable apparatus which physically moves transverse to the conveyor belt in order to lay the pitch yarn uniformly. This movable apparatus is referred to in the art as a "travelling godet" and is rate limited even for z careful design and can damage the pitch yarn because of the tendency-of the pitch yarn to adhere to rolls within the apparatus. Such adhesion is due to surface tension arising from the sizing used to maintain the pitch fibers together to form the pitch yarn. The travelling godet is followed by an apparatus called r "transvector" which draws the pitch yarn off of the last roll in the travelling godet with suction and directs the pitch yarn downward towards the conveyor belt. The transvector is oot rate limited, but the air pressure moving in the vicinity of the pitch yarn can damage the pitch fibers. The transvactor is followed by a "laydown tube" which deposits the pitch yarn in z predetermined pattern onto the conveyor belt. A poor pattern distribution or too high a pile of pitch yarn can produce very high local heating due to the exothermic reaction during the infusibilizing step. The laydown tube is another potential problem because the pitch yarn wet with site occasionally adheres to the side of the tube for r short time and this interferes with the laydown pattern on the conveyor belt. The conveyor belt carries the pitch yarn into a large oven having an oxibizing atmosphere and which has a predetermined heat gradient for infusibilizing the pitch yarn with as little dumage as is consistent with commercial operations. This beat treatment can take as long as several hours. The cost of the oven as well as the energy costs are very hLgh. Subsequently, the infusibilized yarn is pulled from the belt and is accumulated onto bobbins for easy handling and storage. This operation uses what is called a "downstream drive" and can be troublesome because the infusibilized pitch yarn is not much stronger than the pitch yard. The infusibilized pitch yarn must be collected at a rate consistent with the spinning rate. The instant invention eliminate: the need for the travelling godet, the transvector, the conveyor bolt, the large oven and z downstream drive. In a preferred embodiment of the Invention, a spinning apparatus produces e plurality of pitch fibers, for example 2000, and these pitch fibers are drawn together and drawn down while being wound onto a bobbin after being sized with an oxidizing liquid composition. The combination of drawing down the pitch yarn while collecting the yarn onto a bobbin greatly simplifies the operations and eliminates many expensive pieces of equipment. Thereafter, the bobbin loaded with sized pitch yarn is subjected to a heat treatment in c substantially non-reactive atmosphere to produce carbon yarn. No beat treatment in an oxidizing atmosphere is needed for the pitch yarn <RTI ID=16.10> according to the invention in contrast to the prior art which required s heat treatment in oxygen or air or the like before the beat treatment in a substantially non-reactive atmosphere. The carbon yarn produced according to the invention provides a more efficient use of the precursor pitch than carbon yarn produced according to the prior art. The infusibilizing step of the prior art introduces considerable amounts of oxygen into the pitch yarn, as much as 18% of more by weight. During the carbonizating heat trestment, it is believed that some of the oxygen driven off carries along carbon mtoms. As a result, the carbon yarn produced according to the prior art processes is less than 80% by weight of the pitch yarn. In contrast, the carbon yarn produced according to the invention is about 90% by weight of the pitch yarn. Thus, the invention provides z higher yield of product than the prior art besides simplifying the operations needed to produce carbon yarn. The oxidizing liquid composition can serve many functions in addition to its use in the heat treatment. The composition can provide lubrication of the pitch yarn to minimize friction between the pitch yarn and portions of the equipment contacting the pitch yarn during the manufacturing operations. The composition can also provide adhesion between fibers so that the fibers remain together as g yarn. In a praferred embodiment, the oridizing liquid composition comprises an aqueous nitric acid. A concentration of the aqueous nitric acid of 10% to 50% by volume is preferable. but a concentration of 25% to 35% by volute it more preferable. It is preferable to use deionized water in the aqueous nitric acid to avoid introducing any undesirable ions onto and into the pitch fibers. Aqueous nitric acid is relatively inexpensive and Las been found to be excellent in obtaining carbon yarn. The concentration of the nitric acid depends on how long the nitric acid will be on the pitch yarn before the beat treatment is carried out. A concentration of about 25% by volume is suitable for commercial operations for which the time between the application of the nitric acid to the pitch yarn and the beat treatment varies from 1 to 5 days. With regard to the oxidizing liquid composition, reference is had to the aforementioned U.S. patents No. 4,275,051 and No. 4,276,278, both entitled "Spin Size and Thermosetting Aid For Pitch Fibers". The former patent states that the invention "provides a method of treating a multifilament bundle of pitch fibers, rucb as yarn or tow, to prepare such multifilament bundle for furtber 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 o first compound comprising a vLter-soluble oxidizing agent and z Separate second compound comprising a water-soluble surfactant". The other patent features z water-soluble surfactant which is also capable of functioning as an oxidizing agent. Both of these patents used the term "oxidizing agent" as a source of oxygen for the fiber in order to infusibilize the fiber. As used herein, "oxidizing liquid composition" includes a source of oxygen for infusibilizing the fiber. The disclosure of these patents is incorporated herein It is believed that the oxidizing liquid composition can comprise an aqueous acid or z water-soluble oxidizing agent such as a peroxygenated compound. Some water-soluble oxidizing agents compounds include sodium peroxide, potassium peroxide, ammonium peroxide, sodium persulfate, potassium persulfate, amonium persulfate, sodium pyrosulfate, and sodium nitrate. Preferably, aqueous nitric acid is used in the composition. The oxidizing liquid composition of the invention can also comprise carbon black particles or colloidal graphite and c surfactant. The carbon black particles or collodial graphite tend to separate the pitch fibers from each other and thereby minimize the occurrence of "sticking" or fusion between fibers during the heat treatment according to the invention. One of the functions of the surfactant is to maintain z dispersion of the carbon black particles. Mechanical means in accordance with the prior art can be used to maintain a uniform dispersion of the carbon black particles in the composition. The surfactant also improves the flow of the composition over the fibers. It is believed that the surfactant can be water-soluble and can be anionic or nonionic. Such surfactants are well known and typically include tetra-methyl sodium oleste, tetramethyl ammonium oleate, tetramethyl sodium laurate, tetramethyl ammonium laurate, aodium laurate and ammonium laurate. The oxidizing liquid composition can be applied to the pitch fibers using prior art techniques for applying sizing. Preferably, the composition is applied by contacting the pitch yarn with a rotating wheel which passes through the solution and carries a portion of the solution on its surface to the pitch yarn. Such r wheel is often referred to in the art as a "kise wheel" and rotates to minlmize friction with the yarn as well as carrying new solution to the yarn. After the kiss wheel, the yarn can be accumulated for subsequent treatment. The composition can be applied to the pitch yarn by passing the yarn through a bath of the compositton. This has a drawback because high rpeeds can produce fiber damage due to drag in the bath. Another way of applying the composition to the pitch yarn is to spray s mist of the composition onto the pitch fibers before the fibers are gathered to form the yarn in order to improve the distribution of the composition on the fiber. A size of water can be used on the pitch fibers and the yarn wound onto B bobbin while a mist of the composition is sprayed onto the yarn layers being produced on the bobbin. As an alternate, the composition can be applied to the pitch yarn after the yarn bas been accumulated. For example, the pitch fiber can be wound onto z bobbin and tht bobbin with the yarn can be subjected to the composition. This can be carried out simply by placing the bobbin in r bath of the composition. For this case, a relatively loose winding of the yarn will allow the flow of the composition through the winding: more readily and thereby improve the treatment. s bobbin having a plurality of boles has the advantages of allowing the composition to be forced, under pressure, out from the core to the outer layer using en appropriate arrangement so that the fibers near the bobbin are not inadvertently omitted from the treatment. For this treatment it would be desirable to use some sizing on the pitch yarn prior to winding the yarn onto the bobbin. It is convenient to use water for this sizing. A suitable bobbin has been described in U.S. Patent No. 4,351,816. The bobbin can be shaped like a cylinder or a cylinder with end faces. The bobbin will be subjected to elevated temperature in order to carbonize the yarn on the bobbin Accordingly, the bobbin should be made from z material appropriate for the practice of the invention Preferably, the bobbin comprises a cylindrical body made of stainless steel, or z refractory alloy. or caramic, or boron nitride, or more preferably a graphite material. That Is, the bobbin is made from a material which is thermally and mecbanically stable at the temperatures which will be used to carbonize the pitch yarn on the bobbin. The aforementioned patent No. 4*351*816 discloses a method for producing a mesophase based carbon yarn in which thermoset yarn was wound onto s bobbin as described above and subjected to a heat treatment in a substantially non-reactive atmosphere to produce carbon yarn. The pitch yarn which has been contacited with the oxidizing liquid composition reacts and incorporates oxygen thereby. Tests were carried out to determine the range of oxgen pickup in pitch yarn over a period of 0.1 hour to 70 hours. The yarn had 2000 pitch fibers which had an average diameter of 13.5 microns. Nitric acid with a concentration of 25% by volume was used. After the yarn was contacted with the nitric acid. a predetermined time was allowed to elapse at room temperature and thereafter* the yarn was washed with water for this test and dried at 125 C for 16 hours prior to the test for oxygen content. Surprisingly, the range of oxygen pickup was 1.5% to 4.8% by weight for 0.1 hour to 70 hours with most of the oxygen pickup taking place during the first 24 hours. The test points substantially define the following relationship: oxygen pickup in % by wt. =1.2355 log (time in hrs.)+2.5278 Thurs, the variations in the pitch yarn after contact with the nitric acid in this concentration is not expected to have any significant effect on the commercial operations. That is, trested pitch yarn can be stored prior to being carbonized. This ir advantageous in commerclial manufacturing. The heat treatment of the treated pitch yarn can be carried out in batches in z closed volume furnace or as a continuous process using for example z conveyor belt furnace or z so-called "walking beam furnace" in which bobbins can be moved into and out of the furnace continuously. The furnace should be capable of providing sufficient heat to pyrolyze the yarn and allow z substantially non-reactive atmosphere to be maintained so that the yarn is not consumed. The non-reactive atmosphere in the furnace can be nitrogen, argon, belium or the like. For temperatures greater than about 2500-C, argon and helium are preferable. Preferably. the heat treatment is carried out in a completely non-reactive atmosphere established by purging the furnace throughly. It ir believed that a small amount of oxygen would not be harmful, particularly if the temperature was not raised too rapidly It can be appreciated that yarn wet from being treated with oxidizing liquid composition will produce an atmosphere of steam which should be purged before elevated temperature. are reached at which steam is no longer substantially non-reactive. The use of boron or similar graphitizing components could be used in the furnace atmosphere and are considered non-reactive as used herein. In carry out the invention, the furnace was purged of air prior to raising the temperature of the yard. The purging step can be carried out by subjecting the interior of the furnace to o vacuum and then allowing the interior to fill with nitrogen. The heat treatment according to the invention has three broad ranges which are important in deciding z heating schedule for rate of temperature increase. The rate of temperature increase up-to about 4000C should take into account that the pitch fibers do not become completely infusibilized until they reach about 400 C. Too rapid increase in temperature up to 400 C can result in fiber deformation due to softening, fusion between fibers, and or disorientation of mesophase molecules. The temperature increase above 400 C can be at a higher rate, but must take into account that most of the gas loss for the pyrolyzing or carbonizing process occurs as the fibers are heated between about 400 C and about 800 C. Too rapid an increase can result in damage due to evolving gases. The increase in temperature above 800-C can be as great as desired. Typically, the final temperature is from 1300*C to 2700 C depending on the intended use of the carbon yarn. Csnerally, the beat treatment according to the invention is carried out in 9 substantially non-reactive atmosphere and the temperature can be raised from room temperature at a rate of about 100 C per hour until 800 C. Thereafter. the temperature can be increased as fast as desired to a predetermined final temperature. The rate of increase In temperature up to 400 C depends, in part, on the sizing used, contae tine between the pitch yarn and the oxidizing liquid composition, the softening point of the pitch, the diameter of the fibers, and the composition of the pitch Preferably, the heat schadule for the furnace is 25-C per hour from room temperature to about 400 C then 50 C par bour until about 800 C. Thersafter. the temperature can be raised as fast as desired to z predetermined final temperature. Preferably, the pitch yarn is accumulated onto z refractory bobbin. This has the advantage that after the heat treatment the yarn is in z package suitable for storage and shipment to z location for commercial use, as is the practice. The yarn can be wound onto the bobbin with a cross winding or essentially parallel winding The tension can be monitored and controlled in accordance with prior art technology This is particularly important for the situation in which the drawdown is carried out simultaneously with the winding onto the bobbin. EXAMPLES Several examples were carried out to demonstrate the invention and to measure properties of carbon yarn produced by the invention. The pitch fibers for the examples were produced according to conventional melt spinning processes. The mesophase pitch is heated in an extruder above the melting point of the mesophase pitch to obtain a molten mtate. The extruder pushes the molten pitch through a filter to a metering pump in the spin block. The molten pitch passes through a filterpack before reaching the apinnerette cavities. Each spinnerette contains 1,000 or 2,000 boles of 0.3:- diameter and 0.6mm capillary length. As the pitch fibers emerge from the apinnerette plate they are drawn down to about 13 microns and are immediately quenched with nitrogen so that the pitch hardens. Below the quench chamber. a lubricant or size is applied to the filaments. The pitch yarn is wound on a bobbin by r takeup and draw winder at a winding speed of about 200 to 1000 meters per minute. Example 1 A mesophase pitch having a mesophase content of about 78' by weight and a Net tier softening point of about 324.6 C was spun into 2000 filaments according to the conventional spinning process. The pitch fibers were drawndown ro that the average diameter was about 13 microns and all the, fibers were drawn together to fore a pitch yarn. -Nitrlc acid having a concentration of 20% by volume was applied to the rapidly moving pitch yarn using 2 rotating kiss wheels. The acid treated pitch yarn was wound onto a motor driven rotating graphite bobbin which supplied the force necessary to draw down the fibers and sustain the movement of the pitch yarn. The graphite bobbin had a layer of graphite felt on the surface to receive the yarn. The bobbin was 28 centimeters long and had an outside diameter of about 9 centimeters. The yarn was wound in a cross pattern with g tension of about 85 grams. Bach loaded bobbin had a diameter about 14 contimeters and contained approximately 2.5 kilograms (dry weight) of yarn. The composition of the yarn based on a sample which had been dried is as follows: : carbon Sl.SL bydrogen 3.3% aulfur 0.8% nitrogen 2.8' oxygen 11.6% The yarn on the bobbin was given z heat treatment in a nitrogen atmosphere in z furnace@ The furnace was purged with nitrogen for four hours before the temperature was increased. The temperature of the furnace was increased from roon temperature at the rate of 100 C per hour until z temperature of 1300 C was reached and that temperature was maintained for 2 hours. Tbereafter, the furnace was allowed to eool back to room temperature. An analysis of the carbon yarn produced by the heat treatment showed that the carbon fibers compared to the original dried pitch fibers were about 90.5% by weight of the original dried pitch. In addition, the composition of the carbon yarn was determined to be: carbon 98.0% bydrogen 0.1% sulfur 0.8% nitrogen 0.5% oxygen 0.5% The mechanical properties of the yarn were measured and the average carbon fiber had n tensile strength of 1.5A CPa and z Young's modulus of about 152 CPA. It can be Been that the carbon fibers obtained possessed r very high carbon content and such carbon fibers sre useful in production of composites made with carbon yarn. Krample 2 The carbon yarn produced in Example l as a result of shrinkage during the heat treatment had imprints of wind pattern. In order to remove these imprints and improve the carbon yern, the carbon yarn from Kxample s was subjected to a threadline carbonizing furnace having a temperature of 2400 C. The carbon yarn was unwound and ertended between rollers along r linear path through z nitrogen purge seal into s carbonizing furnace and out tbrougb a nitrogen purge seal. The furnace was heated by electrical resistance. Threadline carbonizing is well known in the prior art. For example, see U.S. Patent No. 4,301,136. The carbon yarn was subsequently sized, ried. and wound onto z second spool for storage. Mechanical properties of the resulting carbon fibers were an average fiber tensile strength of 2.03 GPa and an average fiber Young's modulus of 434 CPa. The fibers had an excellent appearance similar to carbon fibers produced by expensive conventional processes. Example 3 A mesophase pitch having a mesophase content of 80% by weight and a Mettler softening point of about 325 C was used to produce 1000 pitch fibers in the conventional spinning apparatus as used in Example 1 with the modifieation of a different spinnerette to produce 1000 pitch fibers. The pitch fibers were coated with an oxidizing liquid solution using r rotating graphite kiss wheel. The solution consisted of 25% by volume mitric acid, 75% by volume deionized water and carbon black in the amount of 20 grams per liter The rate of rotation of the kies wheel was adjusted so that the pitch fibers picked up an amount of the evolution equivalent to about half the weight of the pitch fibers. The pitch fibers were pulled from the spinning apparatus by directing then onto s rotting mandrel (winder) ro that the rotation of the mandrel resulted in the fibers being drwndoun to approximately an average diameter of 13 microns. The mandrel was a graphite bobbin 28 centimeters long, 9 centimeters in diameter* and having a 0.6 centimeters wall thickness. A 0.6 centimeter layer of carbon felt was wrapped around the core of the bobbin. The pitch yarn was wrapped in a crosswind pattern with the yarn having z linear speed of approximately 250 meters per minute. Batch bobbin contained from 0.5 to 1.0 kilograms of pitch yarn. The bobbins containing the moist pitch yarn were placed in sealed plastic containers for 24 bours at a temperature of about 30 C and thereafter removed from the plastic bags and loaded onto n graphite rack. The rack with the bobbins was then placed into an electric induction furnace. The furnace was purged for 4 hours with nitrogen in order to be certain that c substantially non-reactive atmosphere would be present for the earbonization. The nitrogen was supplied continuously to the furnace throughout the heat treatment in order to maintain the non-reactive etmosphers. The temperature was raised 25 C par hour until 400 C. thereafter the temperature was @@raised 50 C per hour until 800 C, and finally the temperature was raised to 13000C in about 1 hour. The final temperature was maintained for 2 hours and the furnace was allowed to cool back to room temperature. The carbon yarn produced by this example was very flexible and easily removed from the bobbin. This indicates that fusion between portions of the yarn did not occur. An analysis of the carbon yarn using scanning photomicrographs showed that less than approximately 5% of the carbon fibers exhibited rome adhesion to adjacent fibers. Carbon yarn produced by prior art processes typically exhibit a level of 10% or more. The carbon yarn of this example showed the imprint of the crosswinding. As in Example 2, a conventional threadline furnace was used with the furnace having s temperature of 24000 C, the line apeed was about 12 meters per minute, and a line tension of approximately 300 grams. The fibers were straightened out and the mechanical properties showed an average fiber tensile strength of 2.34 CPa and an average fiber Young's modulus of 407 CPa. Example 4 The mesophase pitch used in Example 3 as well as the process steps were repeated excopt that the oxidizing liquid solution also contained 0.001% of a surfactant sold by DuPont as FC-170C. The carbom yarn resulting from the heat treatment in the furnace was excellent and had very little sticking between fibers. A subsequent threadline heat treatment at 2400 C resulted in carbon yarn having an average fiber tensile strangth of 2.55 GPa and an average Young's modulus of 345 CPa.

Claims: CLAIMS 1. A process for manufacturing carbon Jars, comprising steps of: spinning pitch into a plurality of continuous fiber; combining the plurality of continuous fibers to form a pitch yarn; treating the pitch yarn with an oxidizing liquid composition; collecting the pitch yarn into z bulk form; and subjecting the treated pitch yarn in bulk form to a heat treatment in a substantially non-reactive atmosphere to produce carbon yarn in bulk form. 2. The process of claim 1, wherein the pitch is mesophase pitch. 3. The process of claim 1, wherein said oxidizing liquid composition comprises aqueous nitric acid having z concentration of from about 10% to about 50S by volume. 4. The process of claim 2, wherein the aqueous nitric acid has a concentration of from about 15% to about 35% by volume. 5. The process of claim 1. wherein the oxidizing liquid composition comprises a dispersion of graphite or carbon black. 6. the process of claim 5, further comprising an aqueous surfactant. 7. The process of claim 1, wherein the oxidizing liquid composition comprises a water soluble oxidizing agent and z water soluble surfactant. a, The process of elaim 1, wherein the pitch fiber is treated with the oxidizing liquid using a kiss wheel. 9. The process of claim 1, wherein the continuous fibers are drawn down due to tension exerted by the step of collecting the pitch yarn into a bulk form. 10 The process of claim 1, wherein the bulk form is pitch yarn on a bobbin 11. The process of claim 1, wherein the pitch yarn is contacted with said oxidizing liquid composition subsequent to the pitch yarn being collected into a bulk form. 12. The process of claim 1, wherein the heat treatment is carried out by raising the temperature of the fiber from room temperature toa predetermined final temperature at a rate which avoids exceeding the softening point of the fiber during the heat treatment. 13. The process of claim 12, wherein the temperature is raised at the rate of lOO0C per hour. 14. The process of claim 12, wherein the temperature is raised from room temperature to about 400 C at the rate of about 25 per bour and then raised to 800 C at the rate of about 50 C per hour. 15. The process of claim 1, wherein a mon-reactive gas is supplied to maintain z substantially non-reactive gas during the heat trestment. 16. The process of claim 15, wherein the mon-reactive ges ia mitrogen. argon, helium or combination of two or more thereof.

Inventors: NELSON, LOREN CARL, SCHULZ, DAVID ARTHUR
Applicants: AMOCO CORPORATION
Application year: 1985
Main classification: D01F9
IPC codes: D01F9