Polymer for producing carbon fiber and carbon fiber produced therefrom
阅读说明：本技术 用于生产碳纤维的聚合物以及由其制造的碳纤维 (Polymer for producing carbon fiber and carbon fiber produced therefrom ) 是由 J·莫斯科维茨 W·雅各布斯 A·塔克 B·哈蒙 于 2019-07-02 设计创作，主要内容包括：本文描述了一种聚合物,其包含衍生自第一单体、典型地丙烯腈的重复单元以及衍生自不同于该第一单体的第二单体的重复单元,其中该第二单体是包含烯键式不饱和有机阴离子和含有C＝N亚胺基团的有机阳离子的化合物；一种用于使用所述聚合物生产碳纤维的方法；以及由其制造的碳纤维。(Described herein is a polymer comprising repeat units derived from a first monomer, typically acrylonitrile, and repeat units derived from a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group; a method for producing a carbon fiber using the polymer; and carbon fibers made therefrom.)
1. A process for the production of a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group, which process comprises reacting an ethylenically unsaturated organic acid, or anhydride thereof, with an organic base containing a C ═ N imine group.
2. The process according to claim 1, wherein the organic cation containing a C ═ N imine group is a guanidinium ion or an acetamidinium ion, an amidinium ion, or a pyrimidinium ion; typically a guanidinium ion.
3. The process according to claim 1 or 2, wherein the organic base containing a C ═ N imine group is guanidine, acetamidine, amidine, or pyrimidine; typically guanidine.
4. The process according to any one of claims 1-3, wherein the ethylenically unsaturated organic acid, or anhydride thereof, is selected from the group consisting of: methacrylic acid, acrylic acid, crotonic acid, itaconic acid, citraconic acid, mesaconic acid, maleic acid, fumaric acid, aconitic acid, vinylsulfonic acid, p-styrenesulfonic acid, methallylsulfonic acid, and 2-acrylamido-2-methylpropanesulfonic acid, anhydrides thereof, and mixtures thereof.
5. The process of any of claims 1-4, wherein the ethylenically unsaturated organic acid is methacrylic acid, acrylic acid, itaconic acid, or mixtures thereof.
6. A polymer comprising repeat units derived from a first monomer, typically acrylonitrile, and repeat units derived from a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group produced according to the process of any one of claims 1 to 5.
7. A process for producing a polymer comprising repeat units derived from a first monomer, typically acrylonitrile, and repeat units derived from a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation comprising a C ═ N imine group, the process comprising copolymerizing the first monomer, typically acrylonitrile, and a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation comprising a C ═ N imine group produced by the process according to any one of claims 1 to 5.
8. The process according to claim 7, wherein the comonomer ratio is 0 to 20%, typically 1 to 5%, more typically 1 to 3%.
9. The process according to claim 7 or 8, wherein the copolymerization is carried out with 2,2' -azobis [2- (2-imidazolin-2-yl) propane ] dihydrochloride as initiator.
10. A method for producing carbon fibers, the method comprising:
a) preparing a polymer solution or a molten polymer;
b) spinning the polymer solution or the molten polymer prepared in step (a); thereby forming carbon fiber precursor fibers;
c) drawing the carbon fiber precursor fibers through one or more drawing and washing baths to produce drawn carbon fiber precursor fibers that are substantially free of solvent; and
d) oxidizing the drawn carbon fiber precursor fibers of step c) to form stabilized carbon fiber precursor fibers and then carbonizing the stabilized carbon fiber precursor fibers, thereby producing carbon fibers;
wherein the polymer solution or molten polymer comprises a polymer according to claim 6 or a polymer made according to the method of any one of claims 7-9.
11. The method of claim 10, wherein step (b) comprises spinning the polymer solution prepared in step (a) in a coagulation bath.
12. The method of claim 10, wherein step (b) comprises processing the molten polymer produced in step (a) through a spinneret.
13. Carbon fibre produced according to any one of claims 10 to 12.
Technical Field
The present disclosure generally relates to a polymer comprising repeat units derived from a first monomer, typically acrylonitrile, and repeat units derived from a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group. The disclosure also relates to a method for producing carbon fibers using the polymer, and carbon fibers made therefrom.
Background
Carbon fibers have been used in a variety of applications because of their desirable properties such as high strength and stiffness, high chemical resistance, and low thermal expansion. For example, carbon fibers may be formed as structural parts that combine high strength and high stiffness while having a significantly lighter weight than metal components with equivalent properties. Carbon fibers are increasingly being used as structural components in composite materials for aerospace and automotive applications, among others. In particular, composite materials have been developed in which carbon fibers serve as reinforcement in a resin or ceramic matrix.
Carbon fibers from acrylonitrile are typically produced through a series of manufacturing steps or stages. Acrylonitrile monomer is first polymerized by: acrylonitrile monomer is mixed with one or more comonomers (e.g., itaconic acid, methacrylic acid, methyl acrylate, and/or methyl methacrylate) and the mixture is reacted with a catalyst to form a Polyacrylonitrile (PAN) polymer. PAN is currently the most widely used precursor for carbon fibers.
Once polymerized, the PAN polymer can be isolated by typical means or provided as a solution (i.e., a spinning "dope"). The PAN polymer can be converted into precursor fibers by a number of methods known to those of ordinary skill in the art including, but not limited to, melt spinning, dry spinning, wet spinning, gel spinning, among others.
In one method (dry spinning), the heated dope is pumped (filtered) through small holes of a spinneret into a heated inert gas column or chamber where the solvent evaporates, leaving solid fibers behind.
In another process (wet spinning), a heated polymer solution ("dope") is pumped through the orifices of a spinneret into a coagulation bath where the dope is coagulated and solidified into fibers. Wet spinning can be further divided into one of the following sub-methods: (1) wet jet spinning, wherein the spinneret is immersed in a coagulation bath; (2) air gap or dry jet spinning, where the polymer jet exits the spinneret and passes through a small air gap (typically 2-10mm) before contacting with the coagulation bath; and (3) gel spinning, wherein the dope is thermally induced to a phase change from a fluid solution to a gel network. In both the dry and wet spinning processes, the fibers are subsequently washed and drawn through a series of one or more baths.
After spinning and drawing the precursor fibers and before they are carbonized, these fibers need to be chemically altered to convert their linear molecular arrangement into a more thermally stable molecular ladder structure. This is accomplished by heating the fibers in air to about 200-300 ℃ (about 390-590 ° F) for about 30-120 minutes. This causes the fiber to absorb oxygen molecules from the air and rearrange its atomic bonding pattern. This oxidation or thermal stabilization step can be performed by various methods, such as by drawing the fiber through a series of heated chambers or passing the fiber through heated rollers.
After oxidation, the stabilized precursor fiber is heated (carbonized) in one or two furnaces filled with an oxygen-free gas mixture to a maximum temperature of about 1000 ℃ to 3000 ℃ (about 1800 ° F to 5500 ° F) for several minutes. As these fibers are heated, they begin to lose their non-carbon atoms in the form of various gases such as water vapor, hydrogen cyanide, ammonia, carbon monoxide, carbon dioxide, hydrogen, and nitrogen. When the non-carbon atoms are expelled, the remaining carbon atoms form tightly bonded carbon crystals aligned parallel to the long axis of the fiber.
The resulting carbon fibers have a surface that does not bond well to the epoxy and other materials used in the composite. In order to give the fibres better binding properties, their surface may be slightly oxidized. The addition of oxygen atoms to the surface provides better chemical bonding properties and also removes weakly bonded crystallites for better mechanical bonding properties. Once oxidized, the carbon fibers may be coated ("sized") to protect them from damage during winding or weaving.
In the continuous manufacture of carbon fibers, the oxidation of the precursor fibers is a time-consuming step. High oven temperatures and slow throughput hinder cost reduction efforts. Several approaches to the problem of slow oxidation are known, including plasma treatment, microwaves, proton irradiation and post-chemical spinning treatments. However, the production feasibility of such processes has not been achieved, and means to control such processes in a continuous manner have not been developed.
Herein, a new strategy for producing carbon fibers is described, which strategy uses a polymer comprising recurring units derived from a first monomer, typically acrylonitrile, and recurring units derived from a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group, and which strategy will address one or more of the disadvantages described above.
Disclosure of Invention
It has been found that the use of a compound comprising an ethylenically unsaturated organic anion and an organic cation comprising a C ═ N imine group as a second monomer in the production of the polymers described herein allows, among other advantages, cost/energy savings and the reduction or elimination of the use of ammonia for the resulting polymer.
Thus, in a first aspect, the present disclosure relates to a process for the production of a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group, the process comprising reacting an ethylenically unsaturated organic acid, or anhydride thereof, with an organic base containing a C ═ N imine group.
In a second aspect, the disclosure relates to a polymer comprising repeat units derived from a first monomer, typically acrylonitrile, and repeat units derived from a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group.
In a third aspect, the present disclosure relates to a process for producing a polymer described herein, the process comprising copolymerizing a first monomer, typically acrylonitrile, and a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group.
In a fourth aspect, the present disclosure relates to a method for producing carbon fibers, the method comprising:
a) preparing a polymer solution or a molten polymer;
b) spinning the polymer solution or the molten polymer prepared in step (a); thereby forming carbon fiber precursor fibers;
c) drawing the carbon fiber precursor fibers through one or more drawing and washing baths to produce drawn carbon fiber precursor fibers that are substantially free of solvent; and
d) oxidizing the drawn carbon fiber precursor fibers of step c) to form stabilized carbon fiber precursor fibers and then carbonizing the stabilized carbon fiber precursor fibers, thereby producing carbon fibers;
wherein the polymer solution or molten polymer comprises a polymer described herein or a polymer made according to the methods described herein.
In a fifth aspect, the present disclosure relates to carbon fibers produced according to the methods described herein.
Drawings
Figure 1 shows a TGA profile of Guanidine Methacrylate (GMA) made according to the present disclosure using different molar ratios of guanidine carbonate to methacrylic acid.
Figure 2 shows TGA curves for Guanidine Itaconate (GIA) made according to the present disclosure using different molar ratios of guanidine carbonate to itaconic acid.
Detailed Description
As used herein, the terms "a/an", "the" or "the" mean "one or more" or "at least one" and are used interchangeably, unless otherwise specified.
As used herein, the term "comprising" includes "consisting essentially of … … (continents of) and" consisting of … … (continents of) ". The term "comprising" includes "consisting essentially of … … (and" consisting of … …) ".
A first aspect of the present disclosure relates to a process for the production of a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group, the process comprising reacting an ethylenically unsaturated organic acid, or anhydride thereof, with an organic base containing a C ═ N imine group.
The reaction between the ethylenically unsaturated organic acid, or anhydride thereof, and the organic base containing a C ═ N imine group is generally carried out by mixing the ethylenically unsaturated organic acid, or anhydride thereof, and the organic base containing a C ═ N imine group in a liquid medium, typically an aqueous medium. For example, in one suitable method, an ethylenically unsaturated organic acid is dissolved in a liquid medium and then an organic base containing C ═ N imine groups is slowly added to the reaction mixture while stirring.
The molar ratio of organic base containing a C ═ N imine group to ethylenically unsaturated organic acid is typically greater than 0.5. In one embodiment, the molar ratio of the organic base containing a C ═ N imine group to the ethylenically unsaturated organic acid is greater than or equal to 1. In another embodiment, the molar ratio of organic base containing a C ═ N imine group to ethylenically unsaturated organic acid is greater than or equal to 2.
Suitable ethylenically unsaturated organic acids include, but are not limited to, methacrylic acid, acrylic acid, crotonic acid, itaconic acid, citraconic acid, mesaconic acid, maleic acid, fumaric acid, aconitic acid, vinylsulfonic acid, p-styrenesulfonic acid, methallylsulfonic acid, 2-acrylamido-2-methylpropanesulfonic acid, and the like.
In another embodiment, the ethylenically unsaturated organic acid is methacrylic acid, acrylic acid, itaconic acid, or mixtures thereof.
As used herein, an anhydride refers to a compound containing one or more- (C ═ O) -O- (C ═ O) -groups. Such groups are formed by a reaction between two carboxylic acid groups that liberates water molecules. The two carboxylic acid groups may be on the same molecule or on different molecules. Anhydrides suitable for the production of compounds comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group include, but are not limited to, the following anhydrides: methacrylic acid, acrylic acid, crotonic acid, itaconic acid, citraconic acid, mesaconic acid, maleic acid, fumaric acid, aconitic acid, vinylsulfonic acid, p-styrenesulfonic acid, methallylsulfonic acid, 2-acrylamido-2-methylpropanesulfonic acid, and the like.
The organic base containing a C ═ N imine group used in the process can be provided in the form of the free base or in the form of a salt. In the case where the organic base is provided in the form of a salt, the organic base is formed in situ when the salt is at least partially dissolved in a liquid medium, typically an aqueous medium. Suitable organic bases containing a C ═ N imine group include, but are not limited to, guanidines, acetamidines, amidines, six membered heterocycles, such as pyrimidines, pyrazines, pyridazines, triazines, and derivatives and isomers thereof; five-membered heterocycles, such as imidazole, 4, 5-dihydro-1H-imidazole, pyrazole, 1,2, 3-triazole, 1,2, 4-triazole, tetrazole, and derivatives and isomers thereof; fused ring systems such as benzimidazoles, indazoles, benzotriazoles, imidazo-pyridines, quinolines, quinazolines, pteridines, and derivatives and isomers thereof.
In embodiments, the organic base containing a C ═ N imine group is a guanidine, acetamidine, amidine, or pyrimidine; typically guanidine.
As will be apparent to the skilled person, the organic cation containing a C ═ N imine group is derived from the organic base used in the reaction.
In embodiments, the organic cation containing a C ═ N imine group is a guanidinium ion or acetamidinium ion, an amidinium ion, or a pyrimidinium ion; typically a guanidinium ion.
The compound formed comprising the ethylenically unsaturated organic anion and the organic cation containing a C ═ N imine group, i.e. the compound dissolved in the solution, or the compound isolated by methods known to those skilled in the art (e.g. by rotary evaporation or distillation to remove the solvent with or without filtration and then drying) can be used as such.
A second aspect of the present disclosure relates to a polymer comprising repeat units derived from a first monomer and repeat units derived from a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation comprising a C ═ N imine group.
The polymer is typically a Polyacrylonitrile (PAN) based polymer. Thus, in embodiments, the repeat unit derived from the first monomer is a repeat unit derived from acrylonitrile.
The repeating units derived from the second monomer are repeating units derived from a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group, typically produced according to the methods described herein.
The polymer may further comprise repeat units derived from other comonomers. Such repeating units may be derived from suitable comonomers including, but not limited to, vinyl-based acids such as methacrylic acid (MAA), Acrylic Acid (AA), and itaconic acid (ITA); vinyl-based esters such as Methacrylate (MA), Ethyl Acrylate (EA), Butyl Acrylate (BA), Methyl Methacrylate (MMA), Ethyl Methacrylate (EMA), propyl methacrylate, butyl methacrylate, β -hydroxyethyl methacrylate, dimethylaminoethyl methacrylate, 2-ethylhexyl acrylate, isopropyl acetate, Vinyl Acetate (VA), and vinyl propionate; vinyl amides such as Vinyl Imidazole (VIM), acrylamide (AAm), and diacetone acrylamide (DAAm); vinyl halides such as allyl chloride, vinyl bromide, vinyl chloride, and vinylidene chloride; ammonium salts of vinyl compounds and sodium salts of sulfonic acids, such as, inter alia, sodium vinylsulfonate, sodium p-styrenesulfonate (SSS), Sodium Methallylsulfonate (SMS), and sodium 2-acrylamido-2-methylpropanesulfonate (SAMPS).
A third aspect of the present disclosure relates to a process for producing a polymer described herein, the process comprising copolymerizing a first monomer, typically acrylonitrile, and a second monomer different from the first monomer, wherein the second monomer is a compound comprising an ethylenically unsaturated organic anion and an organic cation containing a C ═ N imine group.
The polymer may be made by any polymerization method known to those of ordinary skill in the art. Exemplary methods include, but are not limited to, solution polymerization, dispersion polymerization, precipitation polymerization, suspension polymerization, emulsion polymerization, and variations thereof.
One suitable method comprises mixing in a solvent a first monomer, typically AN Acrylonitrile (AN) monomer, and a second monomer, which is a compound described herein comprising AN ethylenically unsaturated organic anion and AN organic cation containing a C ═ N imine group, in which the polymer is soluble, thereby forming a solution. The solution is heated to a temperature above room temperature (i.e., greater than 25 c), for example to a temperature of about 40 c to about 85 c. After heating, an initiator is added to the solution to initiate polymerization. Once the polymerization is complete, unreacted AN monomer is stripped (e.g., by degassing under high vacuum), and the resulting PAN polymer solution is cooled. At this stage, the polymer is in the form of a solution or stock.
Examples of suitable solvents include, but are not limited to, dimethyl sulfoxide (DMSO), Dimethylformamide (DMF)Dimethylacetamide (DMAc), Ethylene Carbonate (EC), zinc chloride (ZnCl)2) Water and sodium thiocyanate (NaSCN)/water.
In another suitable process, a first monomer, typically AN Acrylonitrile (AN) monomer, and a second monomer, which is a compound comprising AN ethylenically unsaturated organic anion and AN organic cation containing a C ═ N imine group, may be polymerized in a medium, typically AN aqueous medium, in which the resulting polymer is sparingly soluble or insoluble. In this way, the resulting polymer will form a heterogeneous mixture with the media. The polymer was then filtered and dried.
Other comonomers may be used for the polymerization. Examples of suitable comonomers include, but are not limited to, vinyl-based acids such as methacrylic acid (MAA), Acrylic Acid (AA), and itaconic acid (ITA); vinyl-based esters such as Methacrylate (MA), Ethyl Acrylate (EA), Butyl Acrylate (BA), Methyl Methacrylate (MMA), Ethyl Methacrylate (EMA), propyl methacrylate, butyl methacrylate, β -hydroxyethyl methacrylate, dimethylaminoethyl methacrylate, 2-ethylhexyl acrylate, isopropyl acetate, Vinyl Acetate (VA), and vinyl propionate; vinyl amides such as Vinyl Imidazole (VIM), acrylamide (AAm), and diacetone acrylamide (DAAm); vinyl halides such as allyl chloride, vinyl bromide, vinyl chloride, and vinylidene chloride; ammonium salts of vinyl compounds and sodium salts of sulfonic acids, such as, inter alia, sodium vinylsulfonate, sodium p-styrenesulfonate (SSS), Sodium Methallylsulfonate (SMS), and sodium 2-acrylamido-2-methylpropanesulfonate (SAMPS).
The comonomer ratio (amount of comonomer(s) to the amount of acrylonitrile) is not particularly limited. However, suitable comonomer ratios are from 0 to 20%, typically from 1% to 5%, more typically from 1% to 3%.
Suitable initiators (or catalysts) for the polymerization include, but are not limited to, azo-based compounds such as, inter alia, azo-bis-isobutyronitrile (AIBN), 2' -azobis [2- (2-imidazolin-2-yl) propane ] dihydrochloride, 2' -azobis (2-methylpropionamidine) dihydrochloride, 2' -azobis [ N- (2-carboxyethyl) -2-methylpropionamidine ] tetrahydrate, 2' -azobis [2- (2-imidazolin-2-yl) propane ], 2' -azobis [ 2-methyl-N- (2-hydroxyethyl) propionamide ], 4' -azobis (4-cyanovaleric acid), 2' -azobis- (2, 4-dimethyl) valeronitrile (ABVN); and organic peroxides such as, inter alia, dilauroyl peroxide (LPO), di-tert-butyl peroxide (TBPO), diisopropyl peroxydicarbonate (IPP).
In the examples, the copolymerization was carried out with 2,2' -azobis [2- (2-imidazolin-2-yl) propane ] dihydrochloride as initiator.
A fourth aspect of the present disclosure relates to a method for producing a carbon fiber, the method comprising:
a) preparing a polymer solution or a molten polymer;
b) spinning the polymer solution or the molten polymer prepared in step (a); thereby forming carbon fiber precursor fibers;
c) drawing the carbon fiber precursor fibers through one or more drawing and washing baths to produce drawn carbon fiber precursor fibers that are substantially free of solvent; and
d) oxidizing the drawn carbon fiber precursor fibers of step c) to form stabilized carbon fiber precursor fibers and then carbonizing the stabilized carbon fiber precursor fibers, thereby producing carbon fibers;
wherein the polymer solution or molten polymer comprises a polymer described herein or a polymer made according to the methods described herein.
In one embodiment, step (a) comprises preparing a polymer solution.
The preparation of the polymer solution may be accomplished according to any method known to one of ordinary skill in the art. One suitable method is the method described herein, wherein the polymer is formed in a medium, typically one or more solvents (such as those already described), in which the polymer is soluble to form a solution.
Another suitable process is the process described herein, wherein the polymer is formed in a medium, typically an aqueous medium, in which the polymer is sparingly soluble or insoluble to form a mixture, the resulting polymer is isolated, e.g., by filtration, and dissolved in one or more solvents (such as those already described) to form a polymer solution.
In another embodiment, step (a) comprises preparing a molten polymer. The preparation of the molten polymer may be accomplished according to any method known to one of ordinary skill in the art. In a suitable method, preparing the molten polymer comprises forming the polymer in a medium, typically an aqueous medium, in which the polymer is sparingly soluble or insoluble to form a mixture, and isolating the resulting polymer, for example by filtration, and then drying. The polymer is then heated until it is in a molten state suitable for processing through a spinneret.
After the polymer solution or the molten polymer is prepared, a carbon fiber precursor fiber is formed by spinning the polymer solution or the molten polymer.
In one embodiment, step (b) comprises spinning the polymer solution prepared in step a) in a coagulation bath. The term "precursor fiber" refers to a fiber comprising a polymeric material that upon application of sufficient heat can be converted to a carbon fiber having a carbon content of about 90% or greater by weight and particularly about 95% or greater.
To make carbon fiber precursor fibers, the polymer solution (i.e., the spinning "dope") is subjected to conventional wet spinning and/or air gap spinning after the bubbles are removed by vacuum. The dope can have a polymer concentration of at least 10 wt%, typically from about 16 wt% to about 28 wt%, more typically from about 19 wt% to about 24 wt% by weight based on the total weight of the solution. In wet spinning, the dope is filtered and extruded through the holes of a spinneret (typically made of metal) into a liquid coagulation bath for the polymer to form filaments. The spinneret orifices determine the desired fiber filament count (e.g., 3,000 orifices for 3K carbon fibers). In air gap spinning, a vertical air gap of 1 to 50mm, typically 2 to 10mm, is provided between the spinneret and the coagulation bath. In this spinning process, the polymer solution is filtered and extruded from a spinneret in air, and the extruded filaments are then coagulated in a coagulation bath.
The coagulating liquid used in the method is a mixture of a solvent and a non-solvent. Typically water or alcohol is used as the non-solvent. Suitable solvents include those described herein. In one embodiment, dimethyl sulfoxide, dimethylformamide, dimethylacetamide, or a mixture thereof is used as a solvent. In another embodiment, dimethyl sulfoxide is used as the solvent. The ratio of solvent to non-solvent and bath temperature are not particularly limited and can be adjusted according to known methods to achieve the desired cure rate of the extruded nascent filaments in coagulation. However, the coagulation bath typically comprises 40 to 85 wt% of one or more solvents, the balance being non-solvents such as water or alcohols. In one embodiment, the coagulation bath comprises 40 wt% to 70 wt% of one or more solvents, with the balance being non-solvents. In another embodiment, the coagulation bath comprises 50 wt% to 85 wt% of one or more solvents, with the balance being non-solvents.
Typically, the temperature of the coagulation bath is from 0 ℃ to 80 ℃. In one embodiment, the temperature of the coagulation bath is from 30 ℃ to about 80 ℃. In another embodiment, the temperature of the coagulation bath is from 0 ℃ to 20 ℃.
In another embodiment, step (b) comprises processing the molten polymer prepared in step (a) through a spinneret to form carbon fiber precursor fibers. In this manner, the molten polymer is pumped through a spinneret appropriately selected by one of ordinary skill in the art to obtain the desired characteristics, such as the desired filament count of the fiber. After exiting the spinneret, the molten polymer is cooled to form carbon fiber precursor fibers.
The drawing of the carbon fiber precursor fiber is performed by transporting the spun precursor fiber through one or more drawing and washing baths, such as rolls. As a first step in controlling fiber diameter, the carbon fiber precursor fiber is conveyed through one or more washing baths to remove any excess solvent and drawn in a hot (e.g., 40 ℃ to 100 ℃) water bath to impart molecular orientation to the filaments. The result is a drawn carbon fiber precursor fiber that is substantially free of solvent.
In embodiments, the carbon fiber precursor fibers are drawn from-5% to 30%, typically from 1% to 10%, more typically from 3% to 8%.
Step c) of the method may further comprise drying the drawn carbon fiber precursor fiber substantially free of solvent, for example on a drying roll. The drying rolls may be comprised of a plurality of rotatable rolls arranged in series and in a serpentine configuration over which the filaments pass sequentially from roll to roll and under sufficient tension to provide filament stretch or relaxation on the rolls. At least some of the rolls are heated by pressurized steam which is circulated internally or by means of electric heating elements within the rolls or rolls. Before drying, a finishing oil may be applied to the drawn fibers in order to prevent the filaments from sticking to each other in downstream processes.
In step d) of the process described herein, the drawn carbon fiber precursor fiber of step c) is oxidized to form a stabilized carbon fiber precursor fiber, and the stabilized carbon fiber precursor fiber is subsequently carbonized to produce a carbon fiber.
During the oxidation stage, the drawn carbon fiber precursor fiber (typically a PAN fiber) is fed under tension through one or more dedicated ovens, each oven having a temperature of from 150 ℃ to 300 ℃, typically from 200 ℃ to 280 ℃, more typically from 220 ℃ to 270 ℃. Heated air was fed into each oven. Thus, in an embodiment, the oxidation in step d) is performed in an air environment. The drawn carbon fiber precursor fibers are conveyed through one or more ovens at a speed of from 4 to 100fpm, typically from 30 to 75fpm, more typically from 50 to 70 fpm.
The oxidation process binds oxygen molecules from the air to the fibers and starts cross-linking of the polymer chains, increasing the fiber density to 1.3g/cm3To 1.4g/cm3. During oxidation, the tension applied to the fiber generally controls the fiber drawing or shrinking at a draw ratio of 0.8 to 1.35, typically 1.0 to 1.2. When the draw ratio is 1, there is no drawing. And when the draw ratio is greater than 1, the applied tension causes the fiber to be drawn. Such oxidized PAN fibers have an infusible trapezoidal aromatic molecular structure, and they are ready for carbonization treatment.
Carbonization results in crystallization of the carbon molecules and thus produces finished carbon fibers having a carbon content greater than 90%. Carbonization of the oxidized or stabilized carbon fiber precursor fibers occurs in an inert (oxygen-free) atmosphere within one or more specially designed furnaces. In an embodiment, the carbonization in step d) is performed in a nitrogen atmosphere. The oxidized carbon fiber precursor fibers are passed through one or more ovens, each oven heated to a temperature of from 300 ℃ to 1650 ℃, typically from 1100 ℃ to 1450 ℃.
In an embodiment, the oxidized fibers are passed through a pre-carbonization furnace that subjects the fibers to a heating temperature of from about 300 ℃ to about 900 ℃, typically about 350 ℃ to about 750 ℃, while exposing them to an inert gas (e.g., nitrogen), followed by carbonization by passing the fibers through a furnace heated to a higher temperature of from about 700 ℃ to about 1650 ℃, typically about 800 ℃ to about 1450 ℃, while exposing them to an inert gas. Fiber tension may be increased throughout the pre-carbonization and carbonization processes. In pre-carbonization, the applied fiber tension is sufficient to control the draw ratio in the range of 0.9 to 1.2, typically 1.0 to 1.15. In carbonization, the tension used is sufficient to provide a draw ratio of 0.9 to 1.05.
Adhesion between the matrix resin and the carbon fibers is an important criterion in carbon fiber reinforced polymer composites. Therefore, during the manufacture of the carbon fiber, a surface treatment may be performed after oxidation and carbonization to enhance such adhesion.
The surface treatment may comprise drawing the carbonized fibers through an electrolytic bath containing an electrolyte such as ammonium bicarbonate or sodium hypochlorite. The chemistry of the electrolytic bath etches or roughens the surface of the fiber, increasing the surface area available for interfacial fiber/matrix bonding and adding reactive chemical groups.
The carbon fibers may then be subjected to sizing, wherein a sizing coating (e.g., an epoxy-based coating) is applied to the fibers. Sizing may be performed by passing the fibers through a sizing bath containing a liquid coating material. Sizing protects the carbon fibers during handling and processing into intermediate forms, such as dry fabrics and prepregs. Sizing also holds the filaments together in the individual tows to reduce fuzz, improve processability and increase interfacial shear strength between the fibers and the matrix resin.
After sizing, the coated carbon fibers are dried and then wound onto a bobbin.
Those of ordinary skill in the art will appreciate that the processing conditions (including the composition of the spinning solution and coagulation bath, the total bath amount, draw, temperature, and filament speed) are correlated to provide filaments of the desired structure and denier. The process of the present disclosure can be carried out continuously.
In a fifth aspect, the present disclosure relates to carbon fibers produced according to the methods described herein.
Carbon fibers produced according to the methods described herein can be characterized by mechanical properties such as tensile strength and tensile modulus according to ASTM D4018 test method.
The methods of the present disclosure and the carbon fibers produced therefrom are further illustrated by the following non-limiting examples.
Examples of the invention
EXAMPLE 1 Synthesis of guanidine methacrylate monomer
Guanidine Methacrylate (GMA) was synthesized as follows. Methacrylic acid (MAA) was dissolved in distilled water in a reaction flask. Guanidine Carbonate (GC) was slowly added to the reaction solution while stirring. Evolution of carbon dioxide gas was observed and the process was continued until the carbon dioxide gas was eliminated.
The synthesis of GMA was carried out at a molar ratio of guanidine carbonate to methacrylic acid of 1:2 (or 0.5) and a molar ratio of 1:1 (or 1).
The GMA product from each experiment was analyzed by thermogravimetric analysis (TGA). TGA was performed on TA instruments DSC Q600 using Universal Analysis 2000. Fig. 1 shows the TGA profile for GMA made using a 1:2 (or 0.5) molar ratio of guanidine carbonate to methacrylic acid and the TGA profile for GMA made using a 1:1 (or 1) molar ratio. As shown in figure 1, better conversion was observed when the mole ratio of GC to MAA was 1:1 instead of 1: 2.
EXAMPLE 2 Synthesis of guanidine itaconate monomer
Guanidine Itaconate (GIA) was synthesized as follows. Itaconic acid (ITA) was dissolved in distilled water in a reaction flask. Guanidine Carbonate (GC) was slowly added to the reaction solution while stirring. Evolution of carbon dioxide gas was observed and the process was continued until the carbon dioxide gas was eliminated. The reaction solvent is removed by rotary evaporation or distillation.
The synthesis of GIA was carried out at a molar ratio of guanidine carbonate to itaconic acid of 1:1 (or 1) and a molar ratio of 2:1 (or 2).
The GIA product from each experiment was analyzed by thermogravimetric analysis (TGA) as in example 1. Figure 2 shows the TGA profile for the GIA made using a 1:1 (or 1) molar ratio of guanidine carbonate to itaconic acid and the TGA profile for the GIA made using a 2:1 (or 2) molar ratio of guanidine carbonate to itaconic acid. As shown in figure 2, better conversion was observed when the GC to ITA molar ratio was 2:1 instead of 1: 1. The effect of removing the solvent by rotary evaporation or distillation is minimal.