Mesophase pitch containing organometallic compounds for spinning into pitch carbon fibers.

专利摘要:

公开号:NL9102053A
申请号:NL9102053
申请日:1991-12-10
公开日:2001-05-01
发明作者:
申请人:Conoco Inc；
IPC主号:

专利说明:

ORGANOMETAL COMPOUNDS CONTAINING MESOPHASE PEAK FOR SPINNING UPTO CARBON FIBERB
1 ♦ Field of the invention
The invention relates to metal-containing carbon fibers and to an improved process for preparing a soluble, aromatic organometallic compound mesophase pitch suitable for the manufacture of carbon fibers. In particular, the invention relates to a process for making high strength carbon fibers that exhibit superior oxidative stabilization properties, tensile strength and modulus properties. The method comprises adding a soluble aromatic organometallic compound to a graphitizable carbonaceous feedstock or controlling the concentration of an aromatic organometallic compound in a graphitizable carbonaceous feedstock and subjecting that carbonaceous feedstock to a leveling heat treatment to prepare an isotropic pitch product containing mesogens and metals from the organometallic compound. The pitch product thus formed is solvent-fractionated with solvents at about atmospheric pressure. Then, the metal-containing mesogens are heated to a temperature high enough to cause melt to prepare a metal-containing mesophase pitch. The resulting metal-containing mesophase pitch is suitable for melt spinning into an artificial fiber product.
In another method, the carbonaceous feedstock is subjected to a heat treatment to prepare an isotropic pitch product containing mesogens. High molecular weight soluble aromatic organometallic fiber compounds are then added to this isotropic pitch product and the resulting mixture is subjected to solvent fractionation to separate metal-containing mesogens.
Also, the isotropic pitch product containing metals from the aforementioned process can be subjected to solvent fractionation under supercritical extraction conditions to prepare a metal-containing mesophase pitch. When supercritical extraction is used, the conditions are such that directly melted mesophase pitch is obtained, making the melting stage of mesogens unnecessary.
2. The state of the art
Methods for preparing metal-containing pitch products and / or carbon fibers are known and are currently used commercially. For example, U.S. Patent No. 3,258,419, issued August 16, 1977, relates to the use of a phosphoric acid and metal catalyst to aid blowing of asphalt materials with air. The catalyst consists of phosphoric acid containing dissolved metals.
U.S. Patent 3,385,915, issued May 28, 1968, discloses a method of making metal oxide fibers, which consists in impregnating a preformed organic polymer material with a metal. Cellulose and rayon are mentioned as suitable organic polymeric materials.
U.S. Patent 4,042,486 issued August 16, 1977 relates to a method of converting pitch into a crystalloid, which method comprises coating solid amorphous pitch particles with a metal or metal salt before bubbling a gas through them and (the material) subject to a leveling heat treatment to prepare a mesophase pitch.
U.S. Patent 4,554,148, issued November 19, 1985, relates to a carbon fiber making process which consists in subjecting a raw raw oil to thermal cracking conditions to obtain a pitch product containing at least 5 wt% mesophase. A pitch substantially free of mesophase is obtained by removing mesophase of a certain particle size from the pitch product. The crude starting material is obtained from a naphthenic base crude or an intermediate crude oil and contains metals.
U.S. Patent 4,600,496, issued July 15, 1986, discloses a process for converting pitch to mesophase in the presence of catalytically effective amounts of oxides, diketones, carboxylates, and carbonyl compounds of certain metals. The mesophase pitch obtained is described as suitable for use in the manufacture of carbon fibers.
U.S. Patent 4,704,333 relates to a process for forming carbon fibers prepared from the pitch described in the aforementioned U.S. Patent 4,600,496. The method consists in that said mesophase is extruded to form fibers, the extruded fibers are cooled and the fibers are subjected to an elevated temperature to carbonate the fibers.
As can be easily determined from the above references, there is an ongoing research effort to establish new and more advanced methods and methods for making various pitch products and carbon dyog fibers with increased oxidative stabilization, tensile strength and modulus properties.
Summary of the invention
The invention relates to metal-containing carbon fibers, metal-containing mesophase pitch and to a method for making that metal-containing mesophase pitch that is easily spinnable into carbon fibers. The method of making the metal-containing mesophase pitch comprises adding a soluble aromatic organometallic compound to a graphitizable carbonaceous starting material. The metal-containing carbonaceous starting material is subjected to a leveling heat treatment to prepare an isotropic pitch product containing mesogens and soluble aromatic organometallic compounds.
The resulting pitch product is subjected to solvent fractionation to separate metal-containing mesogens from the isotropic oil fraction. The mesogens are then heated to a temperature high enough to melt the mesogens and form a mesophase pitch containing about 50 to about 20,000 ppm of metals from the organometallic compounds.
In another process, the graphitizable carbonaceous feedstock is subjected to a leveling heat treatment to prepare an isotropic pitch product containing mesogens, and a soluble, high molecular weight, aromatic organometallic compound is added to the pitch product prior to solvent fractionation. . The organometallic compounds referred to herein can therefore be added to the carbonaceous starting material either before or after the leveling heat treatment.
Solvent fractionation occurs with solvents or solvent mixtures to isolate the desired mesophase formers (mesogens) from the isotropic oils and particulate impurities. Solvent fractionation is performed with liquid solvents at or near atmospheric pressure. Alternatively, the metal-containing isotropic pitch product can be subjected to solvent fractionation at supercritical extraction conditions to prepare a metal-containing mesophase pitch. When supercritical extraction is used, the conditions are such that directly melted mesophase pitch is obtained, eliminating the need for the melting of the mesogens.
The invention provides a metal-containing mesophase pitch that can be easily spun into a carbon product or carbon fiber. The metal-containing mesophase pitch provides fibers with increased oxidative stabilization, tensile strength and modulus properties.
Detailed description of the invention
According to the invention, a soluble aromatic organometallic compound is added to a carbonaceous starting material. The metal-containing carbonaceous starting material is subjected to a leveling heat treatment to prepare an isotropic pitch product containing mesogens and a soluble aromatic organometallic compound. The resulting pitch product is fractionated with solvents to separate metal-containing mesogens. Then, the metal-containing mesogens are heated to a high enough temperature to prepare mesophase pitch containing metals from the soluble aromatic organometallic compound.
It should be noted that some carbonaceous starting materials may contain small or trace amounts of a metal compound. If this is the case, it is desirable to adjust the metal content of the carbonaceous feedstock to the desired concentration. This is accomplished by adding the soluble aromatic organometallic compounds reported herein to the carbonaceous feedstock to adjust the metal content of the carbonaceous feedstock to the desired concentration.
In another method, the starting carbonaceous material can be subjected to a leveling heat treatment to prepare an isotropic pitch product containing mesogens. Soluble, high molecular weight aromatic organometallic compounds are then added to the pitch product before solvent fractionation. The organometallic compounds can be added to the carbonaceous starting material either before or after the leveling heat treatment step.
Solvent fractionation is performed with solvents or solvent mixtures to isolate the desired mesophase formers (mesogens) from isotropic oils and especially impurities. Solvent fractionation is performed with liquid solvents at or near atmospheric pressure. Alternatively, solvent fractionation is carried out under supercritical temperature and pressure extraction conditions to prepare a mesophase pitch product containing organometallic compounds.
The starting carbonaceous materials used in the process of the invention are heavy aromatic petroleum fractions and coal-derived heavy hydrocarbon fractions, preferably including materials referred to as pitch products. All starting materials used are virtually free of mesophase pitch.
The term "pitch" as used herein means petroleum pitch materials, natural asphalt and heavy oils obtained as a by-product from the naphtha cracking industry, high carbon pitch products obtained from petroleum or coal and other substances having properties of pitch materials which are as by-products formed in various industrial preparation processes.
The term "petroleum pitch" refers to the residual carbonaceous material obtained from the thermal and catalytic cracking of petroleum distillates or residues.
The term "anisotropic pitch or mesophase pitch" means pitch containing molecules with an aromatic structure that are interactively associated to form optically ordered liquid crystals.
The term "isotropic pitch" means pitch containing molecules that are not directed to optically ordered liquid crystals. Fibers made from such pitch products have an inferior quality compared to fibers made from mesophase pitch products;
The term "mesogens" means molecules that interact or associate to form mesophase pitch when in a fluid state.
In general, graphitizable starting materials with a high degree of aromaticity are suitable for practicing the present invention. Carbonaceous pitch materials with an aromatic carbon content of about 40 to about 90% determined by nuclear magnetic resonance spectroscopy are particularly suitable for this method. This also applies to high-boiling, highly aromatic streams containing such pitch products or which can be converted into such pitch products.
It should be noted that carbonaceous pitch products or graphitizable starting materials containing a high content of aliphatic components are also suitable for use in this method. Increasing the stabilization using organometallic compounds is particularly effective with starting materials containing a high content of aliphatic components.
By weight, suitable graphitizable starting materials will contain about 88% to about 93% carbon and about 9 to about 4% hydrogen. Elements other than carbon and hydrogen, such as sulfur and nitrogen, to name a few, are normally present in such pitch materials. Generally, the content of those other elements is no greater than about 5% by weight of the starting material. Also, these suitable starting materials will generally have an average molecular weight of the order of about 200 to about 1000.
Generally, any petroleum or coal-derived heavy hydrocarbon fraction can be used as the carbonaceous feedstock in the process of this invention. Suitable graphitizable starting materials in addition to petroleum pitch include heavy aromatic petroleum streams, tar from ethylene cracking plants, coal derivatives, thermal tar products from petroleum, fluid bed catalytic cracking plants residues, and aromatic distillates with a boiling range of 343-510 ° C. The use of petroleum pitch type starting materials is preferred.
The soluble organometallic compounds of this invention can be either naturally occurring or synthetic organometallic compounds. It should be noted that the naturally occurring soluble organometallic compounds are preferably used herein. The naturally occurring, soluble organometallic compounds of this invention are at least partially aromatic and exhibit good thermal stability and are at least partially soluble in aromatic hydrocarbons. In general, they come from the family of the organometallic complexes found in the asphalt fraction of crude oil. The aromatic organic component of the organometallic compounds concerned here includes porphyrins and related macrocyclic compounds with altered porination structures. They also include porphins with added aromatic rings and / or with sulfur and oxygen as well as nitrogen ligands. Preferred organometallic compounds are thermally relatively stable porphyin-type structures that readily dissolve in the carbonaceous starting materials. These compounds often have analyzed aryl substituents. The metal component of the organometallic compounds is a metal or mixture of metals generally selected from the transition metals. Preference is given to metals from groups VII or VIII of the periodic table.
Particularly preferred metals from the above groups include vanadium, nickel, zinc, iron, copper, iridium, manganese and titanium and mixtures thereof. It should be noted that while all of the metals mentioned herein are suitable for use in the invention, vanadium and nickel are highly preferred, with particular preference being given to vanadium.
The applicant does not wish to commit to any theory, but it is believed that the above-described metal complexes form with the aromatic organic component of the organometallic compounds and form chelates substantially soluble in the carbonaceous starting materials used herein.
An example of a source of naturally occurring soluble aromatic organometallic compounds suitable for use in this invention is Mayan (aka MAYA) crude oil. A concentrate1 can be prepared from Mayan crude containing a significant amount of soluble aromatic organometallic compounds.
Representative examples of soluble synthetic organometallic compounds suitable for use include 5, 10, 15, 20 - tetraphenyl - 21H, 23H - porphine vanadium (IV) oxide; 5, 10, 15, 20 - tetraphenyl - 21H, 23H - porphine nickel (II); 5, 10, 15, 20 - tetraphenyl - 21H, 23H, porphine zinc, 5, 10, 15, 20 - tetraphenyl -21H, 23H, porphine cobalt (II) and 5, 10, 15, 20 - tetraphenyl - 21H, 23H - porphine copper and mixtures thereof. The synthetic vanadium organometallic compounds are particularly preferred. These synthetic organometallic compounds are made and marketed by the Aldrich Chemical Company of Milwukee, Wisconsin.
The organometallic compounds described herein, including both naturally occurring and synthetic organometallic compounds, can be incorporated into the carbonaceous starting material in any suitable manner. For example, the organometallic compounds can be added directly to the carbonaceous starting material by dissolving the desired organometallic compound in the desired content or concentration in the carbonaceous starting material.
Also, the organometallic compounds referred to herein can be mixed with suitable solvents to form mixtures of organometallic compounds and solvents which can be easily dissolved in the appropriate carbonaceous starting material at the desired concentration. When a mixture of organometallic compound and solvent is used, the ratio of organometallic compound to solvent will normally be about 0.05: 20 to about 0.15: 10. It should be noted that solvent ratios outside these ranges for the ratios are also suitable.
Solvents suitable for use in forming the mixtures contemplated herein include petroleum based compounds, for example gas oils, benzene, xylene and toluene and mixtures thereof. Of course, the particular solvent to be selected should be chosen so as not to adversely affect the other desired properties of the final carbonaceous starting mixture.
Typically, the organometallic compound is added to the starting carbonaceous material in an amount sufficient to give a mesophase pitch metal concentration prepared from the starting carbonaceous material from about 50 ppm to about 20,000 ppm, especially from about 80 ppm to about 1000 ppm, and preferably about 100 ppm to about 500 ppm of the metals from the organometallic compound in the mesophobic after solvent extraction and melting of the mesogens.
The soluble aromatic organometallic compounds are added to a carbonaceous starting material and the metal-containing starting material is subjected to a leveling heat treatment to prepare an isotropic pitch product containing mesogens and soluble aromatic organometallic compounds. The conditions used for the equalizing heat treatment are well known in the art and include temperatures ranging from about 350 ° C to about 525 ° C, preferably about 370 ° C to about 425 ° C, at a pressure of about 0.01 to 27 atmospheres for about 1 min to about 100 hours, and especially about 5 min to about 50 hours, and preferably about 2 hours to about 10 hours. It may be desirable to adjust the oil content of the pitch-treated heat treatment by removing oil under vacuum at reduced pressure, between about 0.1 and about 75 mm Hg, either during or after the leveling heat treatment. The process of removing oil from carbonaceous feedstock under vacuum is well documented in U.S. Patent 4,219,404, to which it refers in its entirety. It should be noted that the leveling heat treatment is carried out for a sufficiently long time to allow mesogen to form in the starting material, but not for such a long time that more than 5% of the starting material is converted to mesophase.
It may be desirable to contact the metal-containing carbonaceous feedstock with an oxidatively reactive gas during the leveling heat treatment to accelerate the formation of mesogens. The preferred gas for the oxidative treatment of the carbonaceous feedstock is air and nitrogen or a mixture of oxygen and nitrogen in which oxygen accounts for about 0.05 to about 5% of the gas mixture. Other oxidative reactive gases include ozone, hydrogen peroxide, nitrogen dioxide, formic acid vapor and hydrogen chloride vapor. These oxidative reactive gases can be used alone or in admixture with inert gases (non-oxidizing), such as nitrogen, argon, xenon, helium, methane, hydrocarbon-based flue gas and mixtures thereof. Normally, the starting material is contacted with the oxidative reactive gas at a flow rate of about 1.0 to about 20 SCF gas per pound of starting material per hour. The method of contacting the carbonaceous feedstock with an oxidative reactive gas is more fully described in U.S. Patent No. 4,892,642, all of which is hereby referred to.
Relatively low molecular weight organometallic compounds are suitable for use in the process if the organometallic compounds are added to the carbonaceous starting material prior to the leveling heat treatment. These organometallic compounds will participate in the formation of mesogen-inducing equalizing heat treatment and thus in size growth to substantially the correct size of the mesogen during the equalizing heat treatment. Smaller organometallic compounds in the metal-containing starting material are generally incorporated into the mesogens during the leveling heat treatment. Organometallic compounds of relatively high molecular weight need not be present during the leveling heat treatment, but their presence during the leveling heat treatment is suitable for use herein.
When concentrates of naturally occurring aromatic organometallic compounds are added to a graphitizable carbonaceous feedstock and the mixture is subjected to a leveling heat treatment, it is important that the mesogens in the leveled heat treatment thus obtained are graphitizable materials. Therefore, it is desirable that the concentrates be graphitizable carbonaceous materials.
Alternatively, the graphitizable carbonaceous material may be subjected to a leveling heat treatment to prepare an isotropic pitch product containing mesogens and then the soluble aromatic organometallic compound added to the pitch product prior to solvent fractionation. If this path is followed in practice, the soluble aromatic organometallic compound can be either a compound of the natural or synthetic types already described. The soluble aromatic organometallic compounds can be added alone or in the form of concentrates and they can be mixed in any suitable manner with the mesogen-containing isotropic pitch. When the soluble aromatic organometallic compounds are added as naturally occurring concentrates, concentrates with relatively high metal contents above 50 ppm or even above 1000 ppm are preferred. It is not necessary that the concentrate be a graphitizable carbonaceous material, provided that the concentrate does not prevent the mesogens isolated by extraction from being graphitizable. Mayan residue and Mayan crude oil asphaltenes are examples of suitable naturally occurring concentrates for the practice of this aspect of the invention.
If the soluble, aromatic organometallic compounds are added to the pitch product after the leveling heat treatment, it is important to use only high molecular weight organometallic compounds. A significant portion of the high molecular weight organometallic compounds co-precipitate with mesogens from the isotropic pitch during solvent fractionation. The solvent fractionation step of the process is selective for separating and concentrating high molecular weight soluble aromatic organometallic compounds along with the mesogens from the pitch product. Lower molecular weight organometallic compounds remain soluble during the solvent fractionation treatment. It should be noted that suitable high molecular weight organometallic compounds need not be insoluble under conditions under which mesogens precipitate. It is only required that a significant portion of the organometallic compounds coprecipitate with the mesogens. High molecular weight soluble aromatic organometallic compounds suitable for use herein are the organometallic compounds in which a substantial portion has a molecular weight in the range of about 800 to about 2000.
The isotropic pitch product containing mesogens and soluble aromatic organometallic compounds as formed in the leveling heat treatment or mixtures as taught above are subjected to solvent fractionation to form, after melting, a metal-containing mesophase (anisotropic) pitch suitable for spinning to artificial carbon products or carbon fibers. Solvent fractionation is performed by the following steps: (1) fluxing the isotropic pitch product containing mesogens and soluble aromatic organometallic compounds in an aromatic solvent.
(2) Separation of insoluble residues from fluxing by filtration, centrifugation or other suitable means, (3) Diluting the filtrate of the flux treatment with an anti-solvent to a metal-containing mesophase pitch precursor, for example, organometallic compounds containing mesogens, to precipitate, and washing and drying of the mesophase pitch precursor.
The steps of fluxing and removing the insoluble constituents of the solvent fractionation from fluxing can be omitted. This is especially true if the isotropic pitch subjected to solvent fractionation is a clean material as obtained by hot filtration. The best carbon fiber properties are obtained in the preferred aspect of the invention when the isotropic pitch containing mesogens and soluble organometallic compounds is mixed with a solvent before fluxing and fluxed to solubilize the mesogens. All kinds of solvents are suitable for use as the flux material. These include aromatic compounds such as benzene and naphthalene, naphthenoaromatic compounds such as tetraline and 9,10-dihydroanthracene, alkyl aromatic compounds such as toluene, xylenes and methylnaphthalenes, heteroaromatic compounds such as pyridine, quinoline and tetrahydrofuran; and combinations thereof. Also suitable are simple halohydrocarbons, including chlorine and fluorine derivatives of paraffin hydrocarbons having 1 to 4 carbon atoms, such as chloroform and trichloroethane, and halogenated aromatics such as trichlorobenzene. In general, any organic solvent that is non-reactive with the pitch, and which, when mixed in sufficient amount with the pitch, is capable of solubilizing the mesogens, is used in the practice of the method of the invention. At temperatures above about 500 ° C, undesired reactions can take place with or between aromatics in the pitch. Therefore, the solvent should have the required solubilizing action at temperatures below about 500 ° C.
The amount of solvent used for fluxing will vary depending on the temperature at which the mixing takes place and the composition of the pitch. Generally, the amount of solvent used will range from about 0.05 parts by weight of solvent per part by weight of pitch to about 2.5 parts by weight of solvent per part by weight of pitch. Preferably, the solvent to flux to pitch weight ratio will range from about 0.7 to 1 to about 1.5 to 1. The flux operation is usually performed at an elevated temperature and under sufficient pressure to move the system into the liquid condition. During the flux operation, mixing or shaking is performed to help solubilize the mesogens and the organometallic compounds. Usually, the flux operation is performed at a temperature within the range between about 30 and about 150 ° C for a time between about 0.1 and 2.0 hours. However, the boil-up can be performed at temperatures up to the boiling point of the solvent at the pressure of the system.
After the flux stage is completed, the solubilized mesogens and organometallic compounds are separated from the insoluble portion of the pitch by conventional settling, centrifuging or filtration techniques. If filtering is the chosen separation technique employed, a filter aid may be used if desired to facilitate separation of the liquid material from the solids. The solid materials removed from the liquid pitch material consist of materials such as coke and catalyst fines that were present in the pitch prior to the leveling heat treatment, as well as the insolubles formed during the leveling heat treatment. If the equalizing heat treatment conditions are not carefully controlled, mesophase may form in the pitch during the equalizing heat treatment. This mesophase is partly lost in the flux treatment because it is predominantly insoluble in the mixture before fluxing and is removed with the other insoluble components during the separation treatment. In the process of the invention, isotropic pitch which is substantially free of mesophase is preferred because it means that the pretreatment of the pitch has taken place in a manner that provides a maximum amount of mesogens in the pitch prior to fractionation with solvent.
After removing the solids from the system, the residual pitch-solvent mixture containing dissolved mesogens and organometallic compounds is treated with a co-mixture or anti-solvent to precipitate organometallic mesogens from the pitch. The isotropic pitch containing mesogens and organometallic compounds can be contacted with the co-mixture or anti-solvent in a one-step or two-step process.
Preferably, the co-mixture or anti-solvent system comprises a mixture of aromatic hydrocarbons such as benzene, toluene, xylene and the like and aliphatic hydrocarbons such as hexane, heptane, cyclohexane, methylcyclohexane and the like. A particularly favorable co-mixture or anti-solvent is a mixture of toluene and heptane. Generally, the aromatic-aliphatic co-mixture will be admixed in a volume ratio of from about 6: 4 to about 9.1: 0.1. Generally, the co-mixture or anti-solvent is added to the isotropic pitch in a ratio of about 5 ml to about 150 ml of anti-solvent per gram of isotropic pitch. This range of ratios is sufficient to precipitate metal-containing mesogens from the isotropic pitch system. After precipitation of the metal-containing mesogens from the isotropic pitch, separation of the metal-containing mesogens from the isotropic pitch can take place using conventional techniques such as settling, centrifugation, filtration and the like. The solvent fractionation process which includes fluxing with liquids, anti-solvent fluids, ratios of fluxing fluids or anti-solvent fluids to the pitch product formed after the leveling heat treatment are discussed in more detail in U.S. Patents 4,277,324 and 4,277. 325, to the full contents of which reference is made here.
Alternatively, the isotropic pitch can be extracted to yield an insoluble residue consisting of mesophase pitch precursor as taught in U.S. Patent No. 4,208,267. For example, U.S. Patent 4,208,267 discloses a process for preparing mesophase pitch in which a carbonaceous isotropic pitch is extracted with a solvent to give a solvent insoluble fraction with a sintering point below about 350 ° C. The solvent-insoluble fraction is separated from the solvent-soluble fraction and the solvent-insoluble fraction is subjected to a heat treatment to prepare an optically anisotropic pitch. The description of U.S. Patent No. 4,208,267 is hereby referred to as reference.
After the solvent fraction step, the metal-containing mesogens are heated to a high enough temperature to melt the mesogens and form a metal-containing mesophase pitch. The mesogens are heated to temperatures up to 400 ° C, but below the decomposition temperature of those mesogens, to promote mesophase pitch formation. Preferably, the mesogens are heated at 10-30 ° C above their sintering temperature to a temperature from about 230 ° C to about 400 ° C. The metal-containing mesophase pitch so formed generally has a softening temperature of about 230 ° C to about 380 ° C when heated on a heated microscope stage.
Alternatively, the isotropic pitch product containing mesogens and soluble aromatic organometallic compounds from the above-described leveling heat treatment step is subjected to supercritical temperature and pressure extraction conditions to prepare a metal-containing mesophase pitch. If supercritical extraction is used, the solvent should have a critical temperature below about 500 ° C. In the supercritical extraction process, the isotropic pitch product containing mesogens and soluble aromatic organometallic compounds is subjected to supercritical extraction conditions in temperature and pressure to form a metal-containing mesophase pitch. Supercritical extraction is performed by the following steps: (1) Fluxing the isotropic pitch product containing mesogens and soluble aromatic organometallic compounds in an aromatic solvent, (2) separating the insoluble components from the fluxing by filtration, centrifugation or other suitable agents, (3) subjecting the soluble components of the fluxing to supercritical temperature and pressure extraction conditions to prepare a metal-containing mesophase pitch.
The pitch solvent mixture of step (3) containing dissolved mesogens and organo-metal compounds is subjected to supercritical temperature and pressure conditions, i.e. temperature and pressure, at or above the critical temperature and critical pressure of the flux solvent, to phase separate bring the mesogens out of the pitch. In the case of toluene, the critical conditions are, for example, 319 ° C and a pressure of 611 psia (4.2 MPa absolute). The time required to separate mesogens from the system will vary depending on the particular pitch and the solvent used and the geometry of the separation vessel. In general, a time from about 1 min to about 60 min is sufficient to separate mesogens from the system.
If desired, additional solvent can be added, for example during the supercritical extraction. The amount of such an added solvent can be up to about 12 parts by weight of solvent per part by weight of pitch, and preferably about 0.5 to about 8 parts of solvent per part by weight of pitch. When additional solvent is added, shaking or stirring or mixing is desired to promote intimate contact between the phases.
In the prior art isotropic pitch solvent fractionation method involving the use of a co-mixture or ahti-solvent, a melting operation serves to convert the mesogens to mesophobic. In the process of this invention, melting is not necessary to effect this conversion because the product obtained in the supercritical phase separation step is mesophase instead of mesogens.
The supercritical conditions used in carrying out the process of the invention will vary depending on the solvent used, the composition of the pitch and the temperature used. The supercritical pressure level can be used to control the solubility of the pitch in the solvent to determine the yield and melting point of the mesophase product. For example, at a given temperature and solvent to pitch ratio, as the pressure on the system is increased, the solubility of the pitch in the solvent also increases. This results in a lower yield of metal-containing mesophase product with a higher melting point. Decreasing the pressure gives the opposite result. Generally, the supercritical temperature used will be at or slightly above the critical temperature of the solvent, for example, 0 to about 100 ° C above the critical temperature of the solvent. Higher temperatures can be used if desired; however, they are not necessary. The pressure maintained on the system will vary over a wider range as it is most suitably used to control product properties and yield. For example, the pressure applied to the system can be up to twice the critical pressure or even higher if desired.
The temperature and pressure required for the process referred to herein are equal to or higher than the critical temperature and pressure of the solvent used in the process. Suitable solvents are those which have critical temperatures in the range from about 100 ° C to about 500 ° C. The upper temperature limit is determined by the thermal stability of the pitch and / or solvent mixture. The lower temperature limit is set by the critical temperature of the solvent used. Preferred solvents, however, have critical temperatures above about 200 ° C; other solvents, such as the halo-carbon compounds, have lower critical temperatures. For example, chlorotrifluoromethane has a critical temperature of 29 ° C. The temperature at which the process is conducted is generally up to about 100 ° C above the critical temperature of the solvent or even higher. The pressure in the process is generally about 2.07 MPa gauge pressure to about 34.5 MPa gauge pressure, and preferably about 3.45 MPa gauge pressure to about 20.7 MPa gauge pressure. It should be noted, however, that higher or lower pressures may be used for some pitch / solvent systems processes. The system pressure varies over a wide range as it is most suitably used to control product properties and yield. For example, the pressure applied to the system can be up to twice the critical pressure of the solvent or higher.
The amount of solvent used in the process and the temperature used also affect the solubility of the pitch in the solvent which in turn affects the melting point of the metal-containing mesophase product. Increasing the amount of solvent lowers the amount of pitch solubilized at low solvent to pitch ratios (1 to 1) but slightly increases the amount of pitch solubilized at high solvent to pitch ratios (10 to 1). Changes in solvent to pitch ratios leading to a reduced yield give a metal-containing mesophase product with an increased melting point.
After the phase separation of the mesogens (now mesophase) and organometallic compounds from the pitch is completed, the solvent dissolved in the mesophase can be removed by lowering the pressure on the system while keeping the temperature sufficiently high to allow the mesophase to enter the liquid state. Solvent removal is usually performed at a temperature between about 300 and about 400 ° C for about 0.01 to about 2 hours, depending on the type of solvent removal method used. With thin film evaporation, for example, only very short residence times are required.
In addition to conventional solvent fluxing, the method of this invention also includes enhanced fluxing. For enhanced fluxes, elevated temperatures and pressures are used up to the critical conditions for the flux mixture. Enhanced fluxing gives higher solubility leading to improved yields. It also offers process advantages, such as greater compatibility with the supercritical conditions used in the process and easier filtering of flux (medium) from less viscous mixtures. The solvent ratio used in the enhanced fluxing will vary between about 0.5 and 2.5 parts by weight of solvent per part by weight of pitch.
After removing the solvent, the metal-containing liquid mesophase recovered under the supercritical conditions of the invention can be spun directly or alternatively, this material can be cooled to a solid phase material for transport and storage. If desired, the mesophase product can be washed with solvent and dried as in the conventional two-solvent process.
In the preferred aspect of the invention described above, upon fluxing the heat-treated isotropic pitch with solvent and filtering the flux mixture, inorganic impurities and components insoluble in the flux mixture, the desired product is removed. This results in a high-quality metal-containing mesophase with a very low content of substances insoluble in quinoline. Dense phase or supercritical separation of the mesogens and organometallic compounds from the pitch can also take place without the flux or filtration steps to obtain a desired metal-containing mesophase product. Although the metal-containing mesophase obtained by this simplified process is not as high a quality as the product obtained by fluxing and filtering, it is more economical and suitable for use in many applications. In this embodiment of the invention, the isotropic pitch treated with equalizing heat treatment containing organometallic compounds and mesogens is suitably combined with the solvent. For example, the pitch can be melted and combined with heated solvent and the combination can then be subjected to supercritical conditions. Also, the pitch can be subjected to supercritical conditions of the particular solvent used and then combined with solvent which is also added under supercritical conditions. After they have been combined, the pitch and solvent are subjected to mixing or shaking to obtain an intimate mixture of the materials before phase separation. Thereafter, the method used is similar to that previously described for the invention after the filtration step. The solvents used in this embodiment of the invention are the same as those previously mentioned. The amount of solvent used is up to about 12 parts by weight per part by weight of pitch and preferably about 0.5 to about 8.0 parts of solvent per part of pitch.
The mesophase pitch of this invention contains from about 50 ppm to about 20,000 ppm of metals from the soluble aromatic organometallic compound added to the graphitizable carbonaceous feedstock and can be formed into metal-containing copper articles by conventional techniques or by methods such as melt spinning, centrifugal spinning, blow spiders and the like to metal-containing anisotropic carbon fibers are spun. It should be noted that the carbon articles or carbon fibers produced by the said process contain substantially the same metals and the same concentration of metals as stated in the description of the metal-containing mesophase pitch products.
The metals in the melt-spun fibers promote increased reactivity with oxygen during stabilization leading to a higher stabilization rate. The higher rate of stabilization of carbon fibers is important from a commercial point of view, as it allows better control of stabilization reactions under relatively mild stabilization conditions. The end result is significantly improved fiber properties when stabilizing relatively thick bundles of fibers as in commercial operations. In the commercial manufacture of carbon fibers, stabilization is a slow, expensive treatment step. The economy of stabilization is improved by treating fiber bundles with relatively high densities or thick fiber bundles. The ability to increase the size of the bundle is limited by increasing the degree of non-uniform stabilization and deteriorating fiber properties. The metal-containing pitch products that exhibit increased stabilization properties stabilize faster and more uniformly compared to pitch products and fibers that do not contain metals. The higher stabilization rate of the carbon fibers in the process referred to herein promotes uniform, homogeneous stabilization and an increased tensile strength of the fibers. This concept is illustrated in Examples IV and V where the treatment of 1/4 inch (6.35 mm) thick fiber bundles on spools is described.
It should be noted that thin bundles of fibers, such as those used in experimental stabilization on a dish or tray, do not show the improvement in fiber properties resulting from the incorporation of metals. They do show increased oxidative stabilization rates as shown in the examples. Improvement of the properties is not expected, because an even, homogeneous stabilization is easily achieved on these thin fiber bundles.
The advantage of soluble aromatic organometallic compounds for promoting oxidative stabilization occurs independently of the process used to make the soluble aromatic organometallic compounds containing mesophase pitch. The advantage occurs with either extracted or bubbled types of mesophase pitch as shown in the examples.
The articles and fibers involved are carbonized and graphitized using techniques and methods customary in the art. For example, carbonization of the articles or fibers is carried out at a temperature of about 1000 to about 2200 ° C and preferably about 1400 to about 1700 ° C for about 1 to about 60 minutes. If desired, the carbonized fibers can be graphitized by further heating them in an inert atmosphere at a temperature of from about 2200 ° C to about 3200 ° C and preferably from about 2800 ° C to about 3000 ° C for a time from about 1 sec to about 5 min. In some cases, a longer heating period is desired, for example up to 10 more or less. It is noted that some or substantially all of the metals present in the mesophase pitch and / or the carbonized articles made therefrom may evaporate during the graphitiser stage. It is only important that the metals are present during the stabilization or oxygenation step to achieve the stated enhanced benefits. These enhanced benefits of the fibers at issue here are achieved, for example, prior to the graphitization step and the evaporation of some or substantially all of the metals present during the graphitization step does not affect the improved properties imparted to the fibers by the metals during the stabilization step.
The following examples serve to demonstrate the best practice of the invention and are not further considered to be limiting thereof.
Example I
A metal-containing mesophase pitch for melt spinning was prepared by topping off a decanted "mid-continent" oil from a refinery to prepare a residue boiling above 454 ° C. This residue consisted of 91.8% carbon, 6.5% hydrogen, 35.1% carbon residue, and 81.6% aromatic carbon as found by analysis by C13 NMR. The decanted oil residue was subjected to a leveling heat treatment at 393 ° C for 6.3 hours and then freed from oil under vacuum to prepare a leveled heat treatment pitch.
Mayan crude was capped to prepare a Mayan residue (46.8% yield). The concentrated residue was mixed with toluene in a ratio of 1: 1 and the mixture was filtered through a 1.2 μτη fluorocarbon filter (with pores). Toluene was stripped from the concentrated residue. The residue was analyzed by emission spectroscopy and found to contain 970 ppm ash which analysis showed contained more than 90% vanadium oxide.
A mixture of the decanted heat treatment subjected to the equalizing heat treatment (85 wt%) and Mayan residue (15 wt%) was fractionated with solvents in the following manner:
The mixture of decanted oil pitch and Mayan residue was mixed with toluene in a 1: 1 ratio. Celite filter aid (0.15 wt%) was added to said mixture and the mixture was stirred at 110 ° C for 1 hour and filtered. Flux-insoluble components were 7.6% of the pitch mixture.
The flux filtrate was combined with hot solvent co-mixture in a 4 ml co-mixture: 1 g flux filtrate ratio to form a mixture for separation. The co-mixture was a mixture of 4 ml of toluene to 1 ml of heptane. The stirred separation mixture was heated to 90 ° C, held at that temperature for 1 hour, cooled to 30 ° C, held at 30 ° C for 1 hour, and finally filtered to recover the precipitated pitch product. The pitch product was washed with 2.6 cm 3 co-mixture of 15 ° C, followed by 0.75 cm 3 heptane at 22 ° C per gram of the original pitch mixture. Mesogen powder was dried and recovered (19.4% yield).
The product melted at 307 ° C to form a 100% anisotropic mesophase pitch as determined by microscopy with a heated microscope stage. The ash content of the pitch was 90 ppm and this ash contained more than 80% vanadium oxide in emission spectroscopy studies.
The mesophase pitch obtained as product was melt spun into carbon fibers. Spinning was excellent at 335 ° C. Scale-stabilized, carbonized fibers on examination had a tensile strength of 2860 GPa (415 Mpsi) and a tensile modulus of 34 MMpsi. Oxidative DSC of the fibers obtained by spinning was found to have achieved a 29% reduction in the time taken to achieve an oxidation level corresponding to stabilization, compared to the comparative fibers of Example III.
Example II
An equalized heat-treated aromatic pitch was mixed with a crude asphalt fraction from Mayan (oil) and the mixture was fractionated with solvent to make a mesophase pitch for spinning purposes.
The same leveled heat-treated, oil-freed decantation pitch as used in Example I was used in this Example.
Mayan crude was capped (482 ° C) to prepare a Mayan residue (46.0% yield). Mayan asphaltenes were isolated from the Mayan residue as a 35% Richfield pentane insoluble material by dissolving the residue in an equal amount by weight of toluene. Mayan asphaltenes were precipitated by adding 20 g of pentane per gram of residue to the mixture of residue and toluene. The asphaltenes, according to analysis, contain 3000 ppm of ash which was found to consist of more than 90% vanadium oxides in research with emission spectrography.
Solvent fractionation was performed according to the method of Example 1. The pitch feed to the solvent fractionation treatment consisted of 95% heat treated equalizing pitch from decanted oil and 5% from Mayan asphaltenes. The amount of flux-soluble constituents was 6.9% of the pitch plus the Mayan asphaltenes. The volume ratio of the co-mixture of this example was 88 parts toluene to 12 parts heptane. The co-mixture to pitch ratios during the separation and scrubbing steps were similar to those used in Example 1. The product yield was 19.3%. The pitch product was 90% mesophase which melted at 322 ° C as shown by analysis by hot microscope stage microscopy. The ash content of the mesophase pitch was 150 ppm and this ash was found to contain more than 90% vanadium oxide when analyzed by emission spectroscopy.
The mesophase pitch was processed by melt spinning at 340 ° C with excellent results. The stabilized and carbonized fibers from the mesophase pitch melt spinning test had a tensile strength of 2930 GPa (425 Mpsi) and a tensile modulus of 36 MMpsi.
Example III (Comparative example)
The procedure of Example 1 was followed to prepare a mesophase pitch, with the following differences:
The concentrated Mayan residue was not added to the capped decanter "mid-continent" oil from a refinery. The solvent co-mixture was a mixture of toluene and heptane in a volume ratio of 92: 8.
The mesophase pitch showed excellent spinnability at 340 ° C. Tray stabilized, carbonized fibers had a tensile strength of 3068 GPa (445 Mpsi) and a tensile modulus of 34 MMpsi. The time taken to achieve an oxidation degree corresponding to stabilization was 29% longer compared to the time of Example I.
Example IV
A metal-containing mesophase pitch for melt spinning was prepared by a mixture of 3/4 residue of decanted "mid-continent" oil from a refinery boiling above 454 ° C and 1/4 residue of "mid-continent "gas oil with a boiling point of more than 435 * 0 /. The mixture contained concentrated soluble naturally occurring organometallic compounds from oil. According to analysis, the mixture contained 90.2% carbon and 7.5% hydrogen. The mixture was subjected to a smoothing heat treatment at 394 ° C for 7.2 hours and then freed from oil under vacuum.
The pitch subjected to the equalizing heat treatment was fractionated with solvents using the procedure of Example I, except that 6.9 ml of co-mixture was used per gram of pitch. The co-mixture was a mixture of 4 ml of toluene to 1 ml of heptane. The mesogen powder existed after melting at 350 ° C, according to analysis by microscopy with a hot microscope stage from 100% mesophase. The product had a total ash content of 164 ppm, which as determined by X-ray spectroscopy analysis consisted of 129 ppm vanadium oxides and 30 ppm nickel oxides. The mesophase powder showed excellent spinnability at 360 ° C. The stabilized, carbonized fibers when tensile strength was determined had a tensile strength of 3571 GPa (518 Mpsi) and a tensile modulus of 36.5 MMpsi.
The fibers were stabilized in spool-wound bundles with a thickness of 6.35 mm by two-step oxidation. They were heated at 240 ° C in the first site step for a period of 325 min in the presence of 14% oxygen. The stabilization was complete after 30 min of treatment in the second step at 24-15-2490C with 0.5% oxygen. The match test was used to determine if the fibers were stabilized. In this test, the flame of a burning match is played over the fibers. Any melting or through-melting of the fibers indicates incomplete stabilization.
The carbonized fibers were ashed and the ash was analyzed for metals. The equivalent of 229 ppm vanadium oxide was found in the ash.
Example V
(comparative example
The method of Example IV was used to produce a carbon fiber, with the following differences:
The leveled heat-treated pitch was prepared from the residue of a decanted "mid-continent" oil from a refinery boiling above 454 ° C and contained no organometallic compounds. The mesophase powder thus obtained had excellent spinnability and fibers made therefrom had a tensile strength of 2826 GPa (410 Mpsi) and a tensile modulus of 36.5 MMpsi.
When the method of stabilizing the fibers on a spool as described in Example IV was used, the fibers were not stabilized. In other words, the fibers melted when tested with the match test. Extending the treatment in step 2 at 245-249 ° C to 40 min with 14% oxygen plus 15 min with 0.5% oxygen still resulted in unstabilized fibers. Stabilizing the fibers required treatment in step 2 with 14% oxygen for 70 min plus 15 min with 0.5% oxygen.
Example VI
A metal-containing mesophase pitch suitable for melt spinning was prepared by topping off a decanted "mid-continent" oil from a refinery to prepare a residue with a boiling point above 454 ° C. Then 0.2% 5.10.15.2 O-tetraphenyl-21H.2 3H-porphin-evanadium oxide (Aldrich Chemical Company) and 27% toluene as co-solvent were added to the residue. The resulting mixture was refluxed with stirring for 4 hours. After removal of the toluene, the remaining aromatic residue contained 150 ppm of added vanadium (IV) oxide.
The vanadium-infused aromatic residue was subjected to a leveling heat treatment at 400 ° C for 7 hours and then freed from oil under vacuum to prepare a synthetic metal containing leveling heat treatment. This pitch, when analyzed, contained 17.2% tetrahydrofuran insolubles.
The equalized heat treatment, decanted pitch, vacuum-freed from oil, was fractionated with solvents by first fluxing with toluene on an equal weight basis. Celite filter aid (0.15 wt.%) Was added to the flux mixture and the flux mixture was filtered using a 0.2 Pm membrane. The flux filtrate was mixed with co-mixture consisting of a mixture of toluene and heptane in a volume ratio of 90:10 to obtain a separation mixture consisting of 8 rolls of co-mixture per gram of equalized heat treated pitch. The separating mixture was heated to 100 ° C with stirring, kept at 30 ° C for 5 hours and then filtered to recover the precipitated product (19.9% yield). The product so prepared was washed successively with 15 ° co-mixture and 22 ° C heptane. The product, when analyzed by microscopy with a hot microscope stage, was found to consist of 100% mesophase with a melting point of 348 ° C. X-ray analysis indicated that in the mesophase 416 ppm vanadium were present. In addition, the product had an ash content of 542 ppm during analysis, which ash, according to an determination by means of emission spectroscopy, consisted of more than 90% vanadium oxide.
Example VII comparative example
A metal-containing mesophase pitch suitable for melt spinning was prepared by topping off a decanted "mid-continent" oil from a refinery to prepare a residue boiling at more than 454 ° C. The decanted oil residue was subjected to an equalizing heat treatment at 393 ° C for 6.3 hours and then freed from oil under vacuum to prepare an equalized heat treated pitch. This pitch contained 16.4% insolubles in tetrahydrofuran at 24 ° C, using 1 g pitch per 20 ml in tetrahydrofuran.
The equalized heat treatment, decanted pitch, vacuum-freed from oil, was fractionated with solvents by first fluxing with toluene based on equal amounts by weight. During the fluxing, 0.2% 5.10.15.20-tetraphenyl-21H.23H-porphine vanadium (IV) oxide (Aldrich Chemical Company) was added to the flux mixture. Celite filter aid (0.15 wt.%) Was added to the flux mixture and the flux mixture was filtered through a 0.2 µ-pore membrane.
The flux filtrate was then combined with a co-mixture consisting of toluene and heptane in a volume ratio of 88:12, to obtain a separation mixture consisting of 8 ml of co-mixture per gram of pitch. The separating mixture was heated to 100 ° C with stirring, kept at 30 ° C for 5 hours and finally filtered to recover the precipitated product (yield 22.9%). The product obtained was successively washed with a co-mixture of 15 ° C and heptane at 22 ° C. The product was found to contain 90% mesophase with a melting point of 308 ° C by microscopic measurement with a hot microscope stage. The ash content was determined to be 40 ppm, indicating poor transfer of metals to the mesogen fraction.
Example VIII
A vanadium-containing mesophase pitch suitable for melt spinning was prepared by topping off a decanted "mid-continent" oil from a refinery to prepare a residue boiling at more than 454 ° C. This residue was mixed with 0.15% 5.10.15.20-tetraphenyl-21H.23H-porphine vanadium (IV) oxide and 10% toluene as a co-solvent. The metal-containing pitch was subjected to a leveling heat treatment at 385 ° C for 32 hours. Nitrogen was bubbled through the residue at a flow rate of 249 L (standard temperature and pressure) per kg of starting material (4SCF per hour per pound of starting material). The residue product was 100% mesophase with a melting point of 320 ° C in an yield of 23.9%. The obtained mesophase pitch gave a residue of 644 ppm on incineration, which was found to be more than 90% vanadium oxide when analyzed by emission spectroscopy.
The mesophase product was spun into carbon fibers with reasonable spinnability at 360 ° C. The stabilized, carbonized fibers, upon examination, had a tensile strength of 2620 GPa (380 Mpsi) and a tensile modulus of 45 MMpsi. A degree of oxidation corresponding to stabilization was achieved 13% faster with these fibers compared to the comparison fibers of Example IX below.
Example IX (comparative example)
A mesophase pitch suitable for melt spinning was prepared according to the procedure described in Example VIII, with the following difference:
The compound 5.10.15i20-tetraphenyl-21H.23H-porphine vanadium (IV) oxide and toluene as cosolvent was not added to the boiling residue of the uncapped deciduous "mid-continent" oil from a refinery. The resulting pitch product was 100% mesophase, with a melting point of 300 ° C, determined by microscopy on a hot microscope stage, and the yield was 23.0%. The ash content of the mesophase pitch was determined to be less than 5 ppm. The mesophase pitch had good spinnability when spinning to carbon fibers at 320 ° C. The stabilized, carbonized fibers had a tensile strength of 2689 GPa (390 Mpsi) and a tensile modulus of 36 MMpsi.
Example X.
Supercritical extraction of a metal-containing isotropic starting material was performed according to the following procedure:
An isotropic starting material is prepared by subjecting a fraction of decanted oil from an FCC unit boiling above 454 ° C to equalizing heat treatment at 394 ° C for 6 hours.
Mayan crude oil was capped to prepare Mayan residue (46.8% yield). The concentrated residue is mixed with toluene in a ratio of 1: 1 and the mixture is filtered through a 1.2 μl fluorocarbon filter (with pores). Toluene was stripped from the concentrated residue. The residue was analyzed by emission spectroscopy to find that it contained 970 ppm of ash which was found to be more than 90% vanadium oxide.
A mixture of the equalized heat-treated pitch from decanted oil (85 wt%) and Mayan residue (15 wt%) is subjected to solvent fractionation under supercritical conditions, according to the following procedure:
The metal containing leveled heat treated pitch is then fluxed by conventional means by mixing the pitch and flux solvent (toluene) in approximately equal amounts at the reflux temperature of toluene. Flux filtration of the mixture removes particles up to a particle size of less than one micron.
A 2L stirred high pressure autoclave is charged with 570g flux filtrate and 665g toluene. The system is heated to 340 ° C under the self-adjusting pressure and an additional 790 g of toluene are added to increase the pressure to 8.20 MPa absolute. The resulting mixture is stirred at 340 ° C and 8.20 MPa for 1 hour and then it is allowed to settle for half an hour. The bottom phase is recovered and dried (removal of toluene residues). According to the analysis, the dried product was 100% mesophase melting at 335 ° C, measured on a microscope with a hot microscope table. The material is spun into carbon fibers which are stabilized on a scale and carbonized by conventional means.
Example XI
Supercritical extraction of a metal-containing isotropic starting material is performed according to the procedure of Example X, with the following differences:
The starting material consists of a mixture of 3/4 decanted "mid-continent" oil from a refinery (residue boiling above 454 ° C) and 1/4 "mid-continent" gas oil (residue boiling above 435 ° C). The mixture contains soluble naturally occurring organometallic compounds from petroleum. The mixture is subjected to a leveling heat treatment, fluxed and supercritical extraction to prepare a mesophase (product). Carbon fibers from this mesophase (product) show an increased stabilization by oxidation.
Of course, all kinds of modifications and variations of the invention can be applied without departing from the inventive idea and the scope thereof.

权利要求:
Claims (129)
[1]
A method for preparing a soluble metal-containing mesophase pitch, comprising: (a) adding a soluble aromatic organometallic compound to a graphitizable carbonaceous starting material, (b) subjecting to a leveling heat treatment of the metal-containing carbonaceous starting material from step (a) to prepare an isotropic pitch product containing mesogens and soluble aromatic organometallic compounds, (c) solvent fractionation of the pitch product prepared in step (b) to separate mesogens containing from about 50 ppm to about 1000 ppm of metals from the organometallic compound, and (d) heating the mesogens at a high enough temperature to form a metal-containing mesophase pitch.
[2]
The method of claim 1, wherein the metals from the soluble organometallic compound of step (a) are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium and mixtures thereof.
[3]
The method of claim 1 or 2, wherein the metals from the soluble organometallic compound of step (a) are vanadium and nickel.
[4]
The method of claims 1 and 2, wherein the metal from the soluble organometallic compound of step (a) is vanadium.
[5]
A method according to any preceding claim wherein the soluble organometallic compound of step (a) is a metal porphyrin.
[6]
A method according to any one of the preceding claims, wherein the aromatic organic component of the organometallic compound comprises porphyrins, macrocyclic compounds with altered porination structures, porphines with added aromatic rings, porphins with sulfur, oxygen and nitrogen ligands and porphins with fused aryl substituents.
[7]
The method of any preceding claim wherein the soluble organometallic compound of step (a) is a naturally occurring metal porphytin.
[8]
The method of any one of claims 1 to 6 wherein the soluble organometallic compound of step (a) is a synthetic organometallic compound.
[9]
The method of claim 8, wherein the soluble synthetic organometallic compound is 5.10.15.20-tetraphenyl-21H.23H-porphine vanadium (IV) oxide.
[10]
The method of any preceding claim, wherein the mesogens of step (c) contain about 80 ppm to about 1000 ppm of the metals from the organometallic compound.
[11]
The method of claim 10 wherein the mesogens of step (c) contain about 100 ppm to about 500 ppm of the metals from the organometallic compound.
[12]
A method according to any preceding claim, wherein the solvent fractionation treatment of step (c) comprises fluxing the pitch product in a solvent, separating the flux (agent) insoluble ingredients and diluting the flux-soluble ingredients with a anti-dissolution agent to precipitate metal-containing mesogens.
[13]
A method according to any preceding claim wherein the solvent fractionation treatment of step (c) comprises extracting the pitch product with a solvent and recovering insoluble metal-containing mesogens.
[14]
The method of any preceding claim, wherein the mesogens in step (d) are heated to a temperature of up to 400 ° C for up to 10 minutes to effect melting of the mesogens and to form a metal-containing mesophase pitch.
[15]
The method according to any one of the preceding claims, wherein the amount of soluble aromatic organometallic compound in the graphitizable carbonaceous starting material of step (a) is adjusted to a concentration sufficient to provide from about 50 ppm to about 20,000 ppm of the metals from the incorporate organometallic compound into the mesogens after the solvent fractionation treatment of step (c).
[16]
A method for preparing a soluble metal-containing mesophase pitch, comprising: (a) subjecting a graphitizable carbonaceous starting material to a leveling heat treatment to prepare an isotropic pitch product containing mesogens, (b) adding soluble aromatic organometallic compounds high molecular weight mesogen containing isotropic pitch product, (c) fractionating the pitch product from step (b) with solvent to separate mesogens containing from about 50 to about 20,000 ppm of metals from the organometallic compound and (d) heating the mesogens to a temperature sufficient to form a metal-containing mesophase pitch.
[17]
The method of claim 16, wherein 75% of the organometallic compounds have a molecular weight in the range of about 800 to about 2000.
[18]
The method of claim 16 or 17, wherein the metals from the soluble organometallic compound of step (b) are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium, and mixtures thereof.
[19]
The method of claim 18, wherein the metals from the soluble organometallic compound of step (b) are vanadium and nickel.
[20]
The method of claims 16-18 wherein the metal from the soluble organometallic compound of step (b) is vanadium.
[21]
The method of any one of claims 16-20, wherein the soluble organometallic compound of step (b) is a metal porphyrin.
[22]
A method according to any one of claims 16-21, wherein in the aromatic organic component of the organometallic compound comprises porphyrins, macrocyclic compounds with a modified porination structure, porphines with added aromatic rings, porphins with sulfur, oxygen and nitrogen ligands and porphins with fused aryl substituents.
[23]
The method of any one of claims 16-22, wherein the soluble organometallic compound of step (b) is a naturally occurring metal porphyrin.
[24]
The method of any one of claims 16-22, wherein the soluble organometallic compound of step (b) is a synthetic organometallic compound.
[25]
The method of any one of claims 16-24, wherein the mesogens of step (c) contain about 80 to about 1000 ppm of the metals from the organometallic compound.
[26]
26. The method of claim 25 wherein the mesogens of step (c) contain about 100 ppm to about 500 ppm of the metals from the organometallic compound.
[27]
27. The method of any one of claims 16-26, wherein the solvent fractionation of step (c) comprises extracting the pitch product with a solvent and recovering insoluble metal-mesating mesogens.
[28]
The method of any one of claims 16-26, wherein the solvent fractionation of step (c) comprises fluxing the pitch product in a solvent, separating flux-insoluble ingredients and diluting the flux-soluble ingredients with an anti-solvent. precipitating metal-containing mesogens.
[29]
29. Method according to one | of claims 16-28 wherein the mesogens in step (d) are heated to a temperature of up to 400 ° C for a time of up to 10 min to effect melting of the mesogens and to form a metal-containing mesophase pitch.
[30]
A method according to any one of claims 16 to 29, wherein the soluble aromatic organometallic compound in the mesogen-containing isotropic pitch product of step (a) is brought to a sufficient concentration in step (b) to allow the mesogens to after the solvent fractionation of step (c), about 50 to about 20,000 ppm of the metals are taken up from the organometallic compound.
[31]
A method of manufacturing a metal-containing graphitizable carbon fiber, comprising: (a) adding a soluble aromatic organometallic compound to a graphitizable carbonaceous starting material, (b) subjecting to a leveling heat treatment of the metal-containing carbonaceous starting material of step (a) ) to prepare an isotropic pitch product containing mesogens and soluble aromatic organometallic compound, (c) fractionating the pitch product formed in step (b) with solvent to remove mesogens containing from about 50 to about 20,000 ppm of metals from the organometallic compound separating and (d) heating the mesogens to a temperature sufficient to form a metal-containing mesophase pitch, (e) melt spinning the metal-containing mesophase pitch of step (d) to produce metal-containing pitch fibers, (f) stabilizing the metal-containing pitch fibers by oxidation and (g) carbonizing d The metal-containing pitch fibers for producing carbon fibers.
[32]
The method of claim 31 wherein the metals from the soluble organometallic compound of step (a) are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium and mixtures thereof.
[33]
The method of claim 31, wherein the metals from the soluble organometallic compound of step (a) are vanadium and nickel.
[34]
The method of claim 31, wherein the metal from the soluble organometallic compound of step (a) is vanadium.
[35]
The method of claim 31, wherein the soluble organometallic compound of step (a) is a metal porphyrin.
[36]
The process according to claims 31-35, wherein the aromatic organic component of the organometallic compound comprises porphyrins, macrocyclic compounds with a modified porination structure, porphines with added aromatic rings, porphins with sulfur, oxygen and nitrogen ligands and porphins with fused aryl substituents .
[37]
A method according to any one of claims 31-36 wherein the soluble organometallic compound of step (a) is a naturally occurring metal porphyrin.
[38]
38. Method according to one! of claims 31-36 wherein the soluble organometallic compound of step (a) is a synthetic organometallic compound.
[39]
The method of claim 38 wherein the soluble synthetic organometallic compound is 5-10.15.20-tetraphenyl-21H.23H-porphine vanadium (IV) oxide.
[40]
The method of any one of claims 31-39, wherein the mesogens of step (c) contain about 80 to about 1000 ppm of the metals from the organometallic compound.
[41]
41. A method according to claim 40 wherein the mesogens of step (c) contain about 100 ppm to about 500 ppm of the metals from the organometal compound.
[42]
42. Method according to one; of claims 31-41, wherein the solvent fractionation of step (c) comprises extracting the pitch product with a solvent and recovering insoluble metal-containing mesogens.
[43]
The method of any one of claims 31-41, wherein the solvent fractionation of step (c) comprises fluxing the pitch product in a solvent, separating flux-insoluble ingredients and diluting the flux-soluble ingredients with an anti-solvent. precipitating metal-containing mesogens.
[44]
The method of any one of claims 31-43 wherein the mesogens in step (d) are heated to a temperature of up to 400 ° C for a time of up to 10 min to effect melting of the mesogens and form a metal-containing mesophase pitch.
[45]
The process according to any one of claims 31-44, wherein the soluble aromatic organometallic compound in the graphitizable carbonaceous starting material of step (a) is brought to a concentration high enough to allow entry into the mesogens after solvent fractionation of step (c). about 50 to about 20,000 ppm of the metals from the organometallic compound are included.
[46]
A method for manufacturing a graphitizable carbon fiber from a metal-containing mesophase pitch, comprising: (a) subjecting to a leveling heat treatment of a graphitizable carbonaceous feedstock to prepare an isotropic pitch product containing mesogens, (b) adding soluble aromatic organome high molecular weight language compounds on the mesogen-containing isotropic pitch product, (c) solvent fractionation of the pitch product formed in step (b), to separate mesogens containing from about 50 to about 20,000 ppm of metals from the organometallic compound ( d) heating the mesogens to a temperature sufficient to form a metal-containing mesophase pitch, (e) melt spinning the metal-containing mesophase pitch of step (d) to produce metal-containing pitch fibers, (f) stabilizing the metal-containing pitch fibers by oxidation and (g) carbonizing the metal-containing pitch fiber ls to manufacture carbon fibers.
[47]
The graphitizable metal-containing carbon fibers of claim 46, wherein the metals of the organometallic compound are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium, and mixtures thereof.
[48]
The method of claim 46, wherein the metals of the soluble organometallic compound of step (b) are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium or mixtures thereof.
[49]
The method of claim 48 wherein the metals of the soluble organometallic compound of step (b) are vanadium and nickel.
[50]
The method of claim 48, wherein the metal of the soluble organometallic compound of step (b) is vanadium.
[51]
The method of claim 46, 48-50 wherein the soluble organometallic compound of step (b) is a metal porphyrin.
[52]
52. A process according to claims 46, 48-505 wherein the aromatic organic component of the organometallic compound comprises porphyrins, imacrocyclic compounds with a modified porphyrin structure, porphins with added aromatic rings, porphins with sulfur, oxygen and nitrogen ligands and potfins with fused aryl substituents.
[53]
The method of claims 46, 48-52 wherein the soluble organometallic compound of step (b) is a naturally occurring metal porphyrin.
[54]
The method of claims 46, 48-52 wherein the soluble organometallic compound of step (b) is a synthetic organometallic compound.
[55]
The method of any one of claims 46, 48-54, wherein the mesogens of step (c) contain about 80 to about 1000 ppm of the organometallic compound metals.
[56]
The method of claim 55, wherein the mesogens of step (c) contain about 100 ppm to about 500 ppm of the metals from the organometallic compound.
[57]
The method of claim 46, 48-56, wherein the solvent fractionation of step (c) comprises extracting the pitch product with a solvent and recovering insoluble metal-containing mesogens.
[58]
A method according to claims 46, 48-56 wherein the solvent fractionation of step (c) comprises fluxing the pitch product in a solvent, separating flux-insoluble ingredients and diluting the flux-soluble ingredients with an anti-solvent. precipitating metal-containing mesogens.
[59]
The method of any one of claims 46, 48-58 wherein the mesogens in step (d) are heated to a temperature of up to 400 ° C for up to 10 minutes to effect melting of the mesogens and to form a metal-containing mesophase pitch .
[60]
The method of claim 46, 48-59, wherein the soluble aromatic organometallic compound in the mesogen-containing isotropic pitch product of step (a) in step (b) is brought to a concentration sufficiently high to about 50 to about 20,000 ppm of the metals from the organometallic compound after the fractionation with solvents of step (c) into the mesogens.
[61]
61. Soluble organometallic compounds containing mesophase pitch suitable for spinning into carbon fibers and comprising a predominant amount of mesophase pitch and a small amount of soluble organometallic compound.
[62]
The soluble organometallic compounds containing mesophase pitch according to claim 61, wherein the mesophase pitch contains about 50 to about 20,000 ppm of the metals of the organometallic compound.
[63]
The soluble organometallic compound containing mesophase pitch according to claim 61 or 612, wherein the mesophase pitch contains about 80 to about 1000 ppm of the metals from the organometallic compound.
[64]
The soluble organometallic compound containing mesophase pitch according to claims 61-63 wherein the mesophase pitch contains about 100 to about 500 ppm of the metals from the organometallic compound.
[65]
The soluble organometallic compound containing mesophase pitch according to claims 61-64 wherein the metals of the soluble organometallic compound are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium or mixtures thereof.
[66]
A soluble organometallic compound containing mesophase pitch according to any one of claims 61-65, wherein the metals of the soluble organometallic compound of step (a) are vanadium and nickel.
[67]
A soluble organometallic compound containing mesophase pitch according to claims 61-65 wherein the metal of the soluble organometallic compound of step (a) is vanadium.
[68]
A soluble organometallic compound containing mesophase pitch according to any one of claims 61-67 wherein the soluble organometallic compound of step (a) is a naturally occurring metal porphyrin.
[69]
The soluble organometallic compound containing mesophase pitch according to claims 61-67, wherein the soluble organometallic compound of step (a) is a synthetic organometallic compound.
[70]
The soluble organometallic compound-containing mesophase pitch according to claims 61-691, wherein the aromatic organic component of the organometallic compound comprises porphyrins, macrocyclic compounds with a modified porination ring structure, porphines with added aromatic rings, porphines with sulfur, oxygen and nitrogen ligands and porphines with fused aryl substituents. .
[71]
The soluble organometallic compound containing mesophase pitch according to claim 69, wherein the soluble synthetic organometallic compound is 5.10.15.20-tetraphenyl-21H.23H-porphine vanadium (IV) oxide.
[72]
72. Graphitisable, metal-containing, spinnable mesophase pitch containing a small amount of a soluble aromatic organometallic compound and having a softening point of about 230 to about 400 ° C.
[73]
The graphitisable metal-containing spinnable mesophase pitch of claim 72, wherein the mesophase pitch contains from about 50 to about 20,000 ppm of metals from the soluble aromatic organometallic compound.
[74]
The graphitisable metal-containing spinnable mesophase pitch of claim 72 or 73, wherein the mesophase pitch contains about 80 to about 1000 ppm of the metals from the organometallic compound.
[75]
The graphitisable metal-containing spinnable mesophase pitch of claims 72-74 wherein the mesophase pitch contains about 100 to about 500 ppm of the metals from the organometallic compound.
[76]
The graphitisable metal-containing spinnable mesophase pitch of claims 72-75 wherein the metals of the soluble organometallic compound are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium and mixtures thereof.
[77]
The graphitisable metal-containing spinnable mesophase pitch of claims 72-76 wherein the metals of the soluble organometallic compound are vanadium and nickel.
[78]
The graphitisable metal-containing spinnable mesophase pitch of claims 72-76 wherein it is the metal of the soluble organometallic compound vanadium.
[79]
The graphitisable metal-containing spinnable mesophase pitch of claims 72-78 wherein the soluble organometallic compound is a naturally occurring metal porphyrin.
[80]
The graphitisable metal-containing spinnable mesophase pitch of claims 72-78, wherein the soluble organometallic compound is a synthetic metal porphyrin.
[81]
The graphitisable metal-containing spinnable mesophase pitch of claims 72-80, wherein the aromatic organic component of the organometallic compound is porphyrins, macrocyclic compounds with a modified porination structure, porphines with added aromatic rings, porphines with sulfur, oxygen and nitrogen ligands, and porphines with fused aryl substituents.
[82]
82. Graphitisable, metal-containing, carbon fibers in the state formed when spinning with increased reactivity of carbon black> comprising a mesophase pitch containing a small amount of an organometallic compound.
[83]
83. Graphitizable metal-containing fibers such as spinning are produced according to claim 82, wherein the carbon fibers contain about 50 to about 20,000 ppm of metals from the organometallic compound.
[84]
The graphitizable metal-containing carbon fibers in the spun state of claim 82, wherein the carbon fibers contain about 80 to about 1000 ppm of the metals of the organometallic compound.
[85]
The graphitizable metal-containing carbon fibers as produced by spinning according to claim 82, wherein the metals of the organometallic compound are selected from vanadium, nickel, irtagnesium, zinc, iron, copper, iridium, manganese and titanium and mixtures thereof.
[86]
86. Graphitizable metal-containing carbon fibers such as those of spinning have been produced according to claim 82, wherein the metal of the organometallic compound is vanadium and nickel.
[87]
87. Graphitisable metal-containing carbon fibers as produced by spinning according to claims 82-85, wherein the metal of the organometallic compound is vanadium.
[88]
88. Graphitizable metal-containing carbon fibers, such as spun-formed, according to claim 82, wherein the carbon fibers are stabilized.
[89]
The graphitizable metal-containing carbon fibers as produced by spinning according to claim 82, wherein the carbon fibers are carbonized.
[90]
90. Graphitizable metal-containing carbon fibers as produced by spinning according to claim 82, wherein the carbon fibers are graphitized.
[91]
91. A method of preparing a soluble metal-containing mesophase pitch, comprising: (a) adding a soluble aromatic organometallic compound to a graphitizable carbonaceous starting material, (b) subjecting the metal-containing carbonaceous starting material of step ( a) to a leveling heat treatment to prepare an isotropic pitch product containing mesogens and soluble aromatic organometallic compounds, (c) combining the isotropic pitch containing mesogens and soluble aromatic organometallic compound, with a solvent, (d) effecting phase separation of the mesogens and soluble, aromatic organometallic compound of the isotropic pitch under temperature and pressure conditions under which the solvent is supercritical, to prepare metal-containing mesophase pitch, and (e) recovering metal-containing mesophase pitch.
[92]
The method of claim 91, wherein the solvent used in step (c) is selected from the group consisting of aromatics, naphtheno aromatics, alkyl aromatics, heteroaromatic compounds, halogen derivatives of paraffins of 1-4 carbon atoms and halogenated aromatics and mixtures thereof, all of which have critical temperatures below about 500 ° C.
[93]
A method according to claim 91 or 92, wherein the solvent used in step (c) is toluene.
[94]
A method according to claim 91 or 92 wherein the solvent used in step (c) is xylene.
[95]
A method according to claims 91-94 wherein the metals of the soluble organometallic compound of step (a) are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium and mixtures thereof.
[96]
The method of claims 91-95, wherein the metals of the soluble organometallic compound of step (a) are vanadium and nickel.
[97]
The method of claims 91-95, wherein the metal of the soluble organometallic compound of step (a) is vanadium.
[98]
98. The method of claims 91-97 wherein the soluble organometallic compound of step (a) is a metal porphyrin.
[99]
The process of claims 91-98 wherein the aromatic organic component of the organometallic compound comprises porphyrins, macrocyclic compounds with altered porphyrin structures, porphins with added aromatic rings, porphine with sulfur, oxygen and nitrogen ligands and porphins and fused aryl substituents.
[100]
The method of claims 91-99 wherein the soluble organometallic compound of step (a) is a naturally occurring metal porphyrin.
[101]
101. A method according to claim 91-99 wherein the soluble organometallic compound of step (a) is a synthetic organometallic compound.
[102]
The process of claim 91 wherein the soluble synthetic organometallic compound is 5.10.15.20-tetraphenyl-21H.2 3H-paraffin vanadium (IV) oxide.
[103]
The method of claims 91-102 wherein the mesophase pitch of step (c) contains about 80 to about 1000 ppm of the metals from the organometallic compound.
[104]
The method of any one of claims 91-103, wherein the mesophase pitch from step (c) contains about 100 to about 500 ppm of the metals from the organometallic compound.
[105]
The process of claims 91-104 wherein the soluble aromatic organometallic compound in the graphisizable carbonaceous starting material of step (a) is brought to a concentration high enough to provide about 50 ppm to about 20,000 ppm of the metals from the organometallic compound after the phase separation step ( d) to be included in the mesogens.
[106]
106. The method of claims 91-105 wherein the metal-containing mesophase pitch is formed into carbon fibers by melt spinning, followed by stabilization and carbonization of the fibers.
[107]
The process of claim 91 and following wherein the temperature and pressure process conditions are equal to or greater than about 319 ° C and 4.2 MPa (611 psia), respectively.
[108]
The method of claims 91-107, wherein the solvent used in step (c) is toluene.
[109]
109. A method of preparing a soluble, metal-containing mesophase pitch, comprising: (a) subjecting a graphitizable carbonaceous feedstock to a leveling heat treatment to prepare an isotropic pitch product containing mesogens, (b) adding soluble aromatic organome high molecular weight language compounds to the mesogen-containing isotropic pitch product, (c) combining the mesogen-containing isotropic pitch and soluble aromatic organometallic compounds, with a solvent, (d) effecting phase separation of the mesogens and soluble aromatic organometallic compound from the isotropic pitch under solvent supercritical temperature and pressure conditions to prepare a metal-containing mesophase pitch and (e) recovering metal-containing mesophase pitch.
[110]
The method of claim 109 wherein the solvent used in step (c) is selected from the group consisting of aromatic compounds, naphthenoaromatic compounds, alkyl aromatic compounds, heteroaromatic compounds, halogen derivatives of paraffins containing 1-4 carbon atoms and halogenated aromatics and mixtures thereof all of which have a critical temperature below about 500 ° C.
[111]
111. The method of claim 109 wherein the solvent used in step (c) is toluene.
[112]
The method of claim 109, wherein the solvent used in step (c) is xylene.
[113]
The method of claim 109 wherein the metals of the soluble organometallic compound of step (b) are selected from vanadium, nickel, magnesium, zinc, iron, copper, iridium, manganese and titanium and mixtures thereof.
[114]
114. The method of claims 109-113 wherein the metals of the soluble organometallic compound of step (b) are vanadium and nickel.
[115]
The method of any one of claims 109-113 wherein the metal of the soluble organometallic compound of step (b) is vanadium.
[116]
The method of claims 109-115 wherein the soluble organometallic compound of step (b) is a metal porphyrin.
[117]
The process according to claim 109, wherein the aromatic organic component of the organometallic compound comprises porphyrins, macrocyclic compounds with altered porphyrin structures, porphins with added aromatic rings, porphins with sulfur, oxygen and nitrogen ligands and porphins and fused aryl substituents.
[118]
The method of claim 109 wherein the soluble organometallic compound of step (b) is a naturally occurring metal porphyrin.
[119]
119. A method according to claims 109-118 wherein the soluble organometallic compound of step (b) is a synthetic organometallic compound.
[120]
The method of claims 109-119 wherein the mesogens of step (c) contain about 80 to about 1000 ppm of the metals from the organometallic compound.
[121]
The method of claim 120, wherein the mesogens of step (c) contain about 100 to about 500 ppm of the metals from the organometallic compound.
[122]
The method of any one of claims 109-121, wherein the soluble aromatic organometallic compound in the graphitizable carbonaceous starting material of step (b) is added in an amount sufficient to increase the content of the metals from the organometallic compound in the mesogens, after the phase separation of step (d) adjustable from about 50 to about 20,000 ppm.
[123]
The method of claims 109-122 wherein the metal-containing mesophase pitch is melt-spun into carbon fibers, followed by stabilization and carbonization of the fibers.
[124]
The method of claim 109 wherein the temperature and pressure conditions of the method are equal to or greater than 319 ° C and equal to or greater than 4.2 GPa (611 psia).
[125]
The method of claim 109 wherein the solvent used is toluene.
[126]
The method of claim 109 wherein 75% of the organometallic compounds have a molecular weight in the range of about 800 to about 2000.
[127]
127. A method of preparing a soluble metal-containing mesophase pitch, comprising: (a) subjecting an isotropic pitch containing mesogens and a soluble aromatic organometallic compound to a flux treatment with a solvent to solubilize the mesogens and organometallic compound, (b) filtering of the flux mixture to remove insolubles, (c) separating the solubilized mesogens and organometallic compound from the flux solvent under supercritical conditions of temperature and pressure for that solvent to prepare a metal-containing mesophase pitch and (d) recovering metal-containing mesophase pitch.
[128]
The method of claim 127 wherein an additional solvent is added to the flux solvent of step (c).
[129]
129. A method of preparing a soluble metal-containing mesophase pitch, comprising (a) forming a mixture by combining an isotropic pitch containing mesogens and a soluble organometallic compound with a solvent, (b) subjecting it in step (a) formed mixture in a phase separation under supercritical conditions of temperature and pressure for that solvent and (c) recovery of mesophase pitch-containing organometallic compounds.

类似技术:

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公开号 | 公开日 | 专利标题

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NL9102053A|2001-05-01|Mesophase pitch containing organometallic compounds for spinning into pitch carbon fibers.

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US4277324A|1981-07-07|Treatment of pitches in carbon artifact manufacture

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US4303631A|1981-12-01|Process for producing carbon fibers

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EP0480106B1|2001-01-03|Process for isolating mesophase pitch

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US4277325A|1981-07-07|Treatment of pitches in carbon artifact manufacture

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EP0034410B1|1983-06-01|Process for the preparation of a feedstock for carbon artifact manufacture

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US5489374A|1996-02-06|Process for isolating mesophase pitch

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EP0546284B1|2000-03-01|Improved process for the production of mesophase pitch

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JP3062247B2|2000-07-10|Direct production method of organic metal-containing pitch for pitch carbon fiber spinning

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MXPA97003289A|1997-08-01|Process to insulate pez mesofas

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EP0119100A2|1984-09-19|Process for preparing a spinnable pitch product

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US4414096A|1983-11-08|Carbon precursor by hydroheat-soaking of steam cracker tar

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JP3051155B2|2000-06-12|Method for isolating mesophase pitch

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CA2055155C|2002-09-17|Direct process route to organometallic containing pitches for spinning into pitch carbon fibers

同族专利:

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公开号 | 公开日

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GB9126474D0|1998-03-18|

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ES2126414A1|1999-03-16|

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DE4141164C2|2003-03-27|

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JP3002536B2|2000-01-24|

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CA2055092C|2002-01-15|

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ES2126414B1|1999-11-16|

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CA2055092A1|1992-06-15|

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FR2756841B1|1999-02-05|

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DE4141164A1|1998-08-27|

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GB2319780A|1998-06-03|

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US5720871A|1998-02-24|

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GB2319780B|1998-09-23|

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US6270652B1|2001-08-07|

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US5932186A|1999-08-03|

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JPH1112576A|1999-01-19|

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FR2756841A1|1998-06-12|

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法律状态:
2001-05-01| A1C| A request for examination has been filed|

优先权:

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US62831490|1990-12-14|

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