FIELD

[0001] The present invention relates to high temperature composites, such as carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites. The present invention also relates to methods for preparing high temperature composites, such as carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites.

BACKGROUND

[0002] High temperature composites such as carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites, can be useful in areas such as hypersonics, solid/liquid rocket propulsion, and other defense/aerospace applications where ultra high temperature properties are required. Industrial applications can include metal and glass processing and concentrated photovoltaics.

[0003] High temperature composites materials, including carbon composites, carbon ceramic matrix composites and carbon silica composites have been traditionally made utilizing pitch or thermoset resins such as phenolic (such as Hexion Durite SC1008) or epoxy. Precursor parts utilizing these thermoset composites are made by a "hand lay-up" requiring significant manual labor to place thermoset prepregs down. In addition to the time and cost of such labor, this manual effort also leads to human error and low quality in precursor parts. Thermoplastic composite materials have an advantage in their ability to be processed by automated methods, including automated tape placement and 3D printing. Theromplastic tape has additional advantages versus thermoset prepregs in that refrigerated shipment and storage is typically not required.

[0004] A pyrolysis step (thermal treatment) can be used in the production of carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites. The pyrolysis can be implemented to eliminate volatiles and/or non-carbon organic elements in the composites (such as in the polymer matrix) and retain the carbon elements.

[0005] But pyrolysis steps can sometimes take hundreds of hours, with an additional day for graphitization. This process is then repeated several times, leading to long lead times for finished parts. Each additional re-infusion plus pyrolysis cycle is labor intensive and time consuming. Additionally, at each cycle there is the possibility that errors or defects could lead to an unacceptable final object. Therefore, it is desirable to reduce the number of cycles required to achieve a fully dense part. Higher char yields allow this process to be shortened because the part is closer to fully solid after the first pyrolysis cycle thereby lessening the number of needed cycles. Typically phenolic based solutions can only provide char yields of 50- 70%. Many other (non PAEK) thermoplastic solutions provide char yields of less than 65%.

[0006] Defect to be avoided, notably occurring during the pyrolyzing steps, are dimensional changes of the part being pyrolyzed, in particular bloating of the part and/or cracks appearing within the part.

[0007] The inventions described herein, which utilize polyaryletherketones (PAEK) and especially polyetherketoneketones (PEKK), unexpectedly overcome these problems. PAEKs, including PEKK, are high performance semi-crystalline polymers having high melting points, extremely high thermal properties, outstanding chemical resistance and flame resistance, and high modulus and strength. By following embodiments of the invention, it is possible to make carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites using a thermoplastic resin. The thermoplastic resin allows automated methods to make precursors parts thereby saving time and money while improving quality and having unexpectedly high char yields, such as char yields from 70% to 80%, up to 85%, up to 90%, and even up to 95% and higher. Pyrolysis cycles can be sped up as the PAEK materials show a single decomposition point thereby alleviating the need for long hold cycles at multiple temperatures often seen with thermoset resins. The surprisingly high char yields also enable fewer pyrolysis/infusion steps than other methods, thereby savings days and even weeks of production time. In certain embodiments, the carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites can be made in a total process time of less than about 50h, 60h, 70h, 80h, 90h, lOOh, HOh, 120h, 130h, 140h, 150h, 160h, 170h, 180h, 190h, 200h, or any ranges between the specified values.

[0008] The Applicant has also surprisingly discovered that according to the embodiments of the invention, it is possible to utilize carbon carbon composite, carbon ceramic matrix composite, and carbon silica composite precursors that combine the advantages of easy processability, high char yields, and high mechanical performance.

[0009] The Applicant has also surprisingly discovered, that in some embodiments, it is possible to utilize carbon carbon composite, carbon ceramic matrix composite, and carbon silica composite precursors that combine the advantages of high char yields and high mechanical performance of PAEK polymers with low dimensional changes of the part being pyrolyzed.

SUMMARY

[0010] The invention is directed to a method for making a high temperature composite, which is a carbon carbon composite, a carbon ceramic matrix composite, or a carbon silica composite, comprising: a. making a precursor part from a resin comprising a polyaryletherketone (PAEK) and at least one reinforcing additive; b. pyrolyzing the precursor part to a pyrolyzed part; c. infusing a liquid second resin into the pyrolyzed part to make an infused part; d. pyrolyzing the infused part to make the carbon carbon composite, the carbon ceramic matrix composite, or the carbon silica composite, and e. optionally repeating steps c. through d. one or more times. During said pyrolyzing, a temperature within a chamber increases one or more times at a rate from 1 °C/h to about 20 °C/h , and is optionally maintained for a period of time at one or more temperatures.

[0011] In one embodiment of the invention, the PAEK comprises one or more of polyetherketoneketone (PEKK), polyetheretherketone (PEEK), polyetheretherketone- polyfether diphenyl ether ketone) (PEEK-PEDEK), polyetherketone (PEK) and polyetherketonetherketoneketone (PEKEKK), preferably PEKK.

[0012] In one embodiment, the PAEK comprises a polyetherketoneketone.

[0013] In one embodiment, the polyetherketoneketone has a T:l isomer ratio of from 50:50 to 78:22, and preferably from 55:45 to 75:25.

[0014] In one embodiment of the invention, the temperature within the chamber increases to a peak temperature of about 1000°C or more during the pyrolyzing.

[0015] In one embodiment of the invention, the liquid second resin comprises one or more of pitch, benzoxazines, furfural, polyester, vinylester, acrylic, and phenolics, preferably pitch and/or phenolics. [0016] In one embodiment of the invention, the precursor part is made by melt processing the resin comprising a polyaryletherketone (PAEK) and the at least one reinforcing additive. The melt processing may comprise one or more of injection molding, extrusion, roto-molding, compression molding, pultrusion, filament winding, and fused filament fabrication printing.

[0017] In embodiments of the invention, the reinforcing additive may comprise one or more of a carbonaceous additive, a chopped fiber, an inorganic additive, or mixtures thereof. The reinforcing additive may comprise a carbonaceous additive being one or more of carbon fiber, carbon nanotubes, graphite, graphene, carbon whisker, a fullerene, carbon black, carbon flake, buckyballs and mixtures thereof. The reinforcing additive may comprise a chopped fiber being one or more of carbon, glass, silica, boron, natural fibers, polymeric fibers and mixtures thereof. The reinforcing additive may notably be chopped carbon fibers or chopped glass fibers. The reinforcing additive may comprise an inorganic additive being one or more of a group IV, V, or VI carbide, silicide, boride, or nitride, and/or ceramic whiskers. The precursor part may comprise a dispersing agent being an organosilicate, oganozirconate, organoaluminate or oraganotitanate.

[0018] The invention is also directed to an embodiment whereby the precursor part of step a. is made by: al) impregnating a continuous fiber tape or fabric with the resin comprising a polyaryletherketone (PAEK) and the at least one reinforcing additive to make a filled PAEK tape or fabric or, co-weaving a continuous fiber or fabric with a PAEK fiber comprising PAEK and the at least one reinforcing additive to make a filled co-woven PAEK fiber or fabric; and a2) processing the filled PAEK tape or fabric or co-woven PAEK fiber or fabric via one or more the following methods: hand-layup, automated tape placement, 3D printing, filament winding, needle punching, and other methods of Z-axis reinforcement followed by one or more compression molding, vacuum bag consolidation, autoclave consolidation, and in-situ consolidation, to make the precursor part. The continuous fiber tape or fabric may comprise carbon fiber or glass fiber.

[0019] In another embodiment the precursor part of step a. is made by: al) processing aligned reinforcing additives and the resin comprising a polyaryletherketone (PAEK) to make an aligned reinforcing additives PAEK, aligned 1-2 dimensional flake material, or aligned 1- 2 dimensional platelet material, to make a fabric, prepreg, or tape comprising the aligned reinforcing additives and impregnated PAEK; and a 2) processing the PAEK tape, prepreg, or fabric via one or more of the following methods: hand-layup, automated tape placement, 3D printing, filament winding, needle punching and other methods of Z-axis reinforcement followed by one or more of compression molding, vacuum bag consolidation, autoclave consolidation, and in-situ consolidation to make the precursor part. The reinforcement additive may be aligned by shear from the melt processing. The aligned reinforcing additives may be made by stretching unidirectional tape until fibers within the aligned reinforcing additives are broken, subjecting the fibers within the aligned reinforcing additives to fluid flow to align the fibers, or subjecting the fibers within the aligned reinforcing additives to electro-magnetic fields to align the fibers.

[0020] The invention further relates to a carbon carbon composite, carbon ceramic matrix composite, or carbon silica composite made by the methods described and claimed herein.

BRIEF DESCRIPTION OF THE FIGURE

[0021] FIG. 1 depicts a PEKK sample with 40% chopped carbon fiber after initial pyrolysis having a char yield of 84%.

DETAILED DESCRIPTION

[0022] Embodiments of the disclosure relate to methods for preparing high temperature composites, such as carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites. Embodiments of the disclosure also relate to carbon carbon composites, carbon ceramic matrix composites, and carbon silica composites made by the disclosed methods.

[0023] As used herein, the term "about" means ±10 % of the noted value. By way of example only, at least "about 50 percent" could include from at least 45 percent to and including at least 55 percent.

[0024] The word "comprising" is used in a manner consistent with its open-ended meaning, that is, to mean that a given product or process can optionally also have additional features or elements beyond those expressly described. It is understood that wherever embodiments are described with the language "comprising," otherwise analogous embodiments described in terms of "consisting of" and/or "consisting essentially of" are also contemplated and within the scope of this disclosure.

[0025] As used herein, the term "aligned" means where >75% of objects have at least one of their major axis oriented (±5°) in the same direction, as measured using images from optical microscopy of cross sections of the composites.

[0026] As used herein, the term "char yield" refers to residual carbon content measured by weight remaining after pyrolysis, and can be determined as set forth in the Example herein.

[0027] As used herein in the context of the composite, the term "% solid" means the percent (%) of density of pyrolyzed part compared to a theoretical fully dense part containing no vacancies or voids. The density of the fully dense part can be calculated by the Rule of mixtures of the matrix material (carbon or ceramic) and the fibrous material (glass or carbon).

D=dla+d2(l-a)

Where

D= density of the fully dense part dl= density of the fibrous material (glass or carbon) a= weight fraction of the fibrous material (glass or carbon) d2=density of the matrix material (carbon or ceramic)

The density of the pyrolyzed part can be experimentally measured by dividing its mass by its volume.

[0028] As used herein, the term "composite" means material comprising at least two different and/or distinct components. For example and without limiting, carbon-carbon composites may comprise a carbon matrix (e.g., graphitic) with carbon fibers. A carbon ceramic matrix composite may comprise a ceramic matrix (e.g., SiC) with carbon. A carbon silica composite can comprise a carbon (typically graphitic) matrix with glass/silica fibers.

[0029] As used herein, the term "high temperature", when used in the expression high temperature composite, means and refer to a temperature of or above about 1000°C, at which the composite is able to be used without detrimental degradation, [0030] As used herein, the term "pyrolyzing" means to enact a chemical change to a material via the application of heat, causing some, substantially all, or all non-carbon or noninorganic elements of the materials to volatize away. In the present invention, the chemical change of the precursor generally occurs at a temperature of at least 250°C, and notably at a temperature of at least 400°C.

[0031] As used herein, the term "infuse" (or "infusing") means to cause a matrix to be penetrated with a liquid resin, and can fill in voids or vacancies.

[0032] As used herein, the term "chopped" refers to fibers that are not continuous and have lengths of about < 20 mm, preferably of about < 15 mm, preferably of about < 10 mm and most preferably of about < 5mm.

[0033] As used herein, the term "polyaryl ether ketone", known by its acronym "PAEK", includes repeating units having the following formulae:

(-Ar-X-) and (^rt-Y-), in which:

- Ar and Ari each denote a divalent aromatic radical;

- Ar and Ari may preferably be chosen from 1,3-phenylene, 1,4-phenylene, l,l'-biphenylene divalent in positions 3,3', l,l'-biphenyl divalent in positions 3,4', 1,4-naphthylene, 1,5- naphthylene and 2,6-naphthylene;

- X denotes an electron-withdrawing group; it may preferably be chosen from the carbonyl group and the sulfonyl group;

- Y denotes a group chosen from an oxygen atom, a sulfur atom or an alkylene group, such as - (CHz)- and isopropylidene.

In these units X and Y, at least 50%, preferably at least 70% and more particularly at least 80% of the groups X are a carbonyl group, and at least 50%, preferably at least 70% and more particularly at least 80% of the groups Y represent an oxygen atom. [0034] According to a preferred embodiment, 100% of the groups X may represent a carbonyl group and 100% of the groups Y may represent an oxygen atom.

[0035] Advantageously, the PAEK(s) may be chosen from:

- a polyether ketone ketone, also known as PEKK; a PEKK comprises one or more repeat units of formula: -Ph-O-Ph-C(O)-Ph-C(O)-;

- a polyether ether ketone, also known as PEEK; a PEEK comprises one or more repeat units of formula: -Ph-O-Ph-O-Ph-C(O)-;

- a polyether ketone, also known as PEK; a PEK comprises one or more repeat units of formula: - Ph-O-Ph-C(O)-;

- a polyether ether ketone ketone, also known as PEEKK; a PEEKK comprises one or more repeat units of formula: -Ph-O-Ph-O-Ph-C(O)- Ph-C(O)-;

- a polyether ether ether ketone, also known as PEEEK; a PEEEK comprises one or more repeat units of formula: -Ph-O-Ph-O-Ph-O- Ph-C(O)-;

- a polyether diphenyl ether ketone, also known as PEDEK; a PEDEK comprises one or more repeat units of formula: -Ph-O-Ph-Ph-O-Ph-C(O)-;

- and mixtures thereof; and

- copolymers comprising at least two of the abovementioned repeat units, in which: Ph represents a phenylene group and -C(O)- represents a carbonyl group, each of the phenylenes possibly being, independently, of the ortho (1-2), meta (1-3) or para-(l-4) type, preferentially being of meta or para type.

[0036] In particular embodiments, the PAEK may be a PEKK essentially consisting of, or consisting of, a terephthalic repeating unit and an isophthalic repeating unit, the terephthalic repeating unit having the formula ("T unit"): the isophthalic repeating unit having the formula ("I unit"):

[0037] For a polymer of a given family, the term "essentially consisting of repeating unit(s)" means that the repeating unit(s) represent a molar proportion of from 95% to 99.9% in the polymer. In addition, the term "consisting of repeating unit(s)" means that the repeating unit(s) represent a molar proportion of at least 99.9%, ideally of 100%, in the polymer.

In particular embodiments, the PAEK may be a polymer consisting essentially of, or even consisting of: a repeat unit of formula: [0038] In particular embodiments, the PAEK may be a polymer consisting essentially of, or consisting of: a repeating unit of formula: and a repeating unit of formula:

[0039] In particular embodiments, the PAEK may be a polymer consisting essentially of, or consisting of the repeating unit of formula (III).

Method comprising melt processing

[0040] In certain embodiments, the present disclosure is directed to a method for preparing a carbon carbon-composite, a carbon ceramic matrix composite, or a carbon silica composite.

[0041] In certain embodiments, the method for preparing a carbon-carbon composite, a carbon ceramic matrix composite, or a carbon silica composite comprises: a. making a precursor part from a resin comprising a polyaryletherketone (PAEK) and at least one reinforcing additive, b. pyrolyzing the precursor part to make a pyrolyzed part, c. infusing a liquid second resin into the pyrolyzed part to make an infused part, and d. pyrolyzing the infused part to make the carbon-carbon composite, the carbon ceramic matrix composite, or the carbon silica composite, and e. optionally repeating steps (c) through (d) one or more times.

[0042] In certain embodiments, the present disclosure is directed to the carbon-carbon composite, carbon ceramic matrix composite, or carbon silica composite made by the method above.

[0043] In certain embodiments, the method can comprise making a precursor part by melt processing. In certain embodiments, the melt processing can be one or more of injection molding, extrusion, roto-molding, compression molding, pultrusion, filament winding and fused filament fabrication printing. In certain embodiments, the melt processing can optionally be followed by melt forming, such as thermoforming or rod bending.

[0044] In certain embodiments, the PAEK can be one or more of polyetherketoneketone (PEKK), polyetheretherketone (PEEK), polyetheretherketone-polyfether diphenyl ether ketone) (PEEK-PEDEK), polyetherketone (PEK) and polyetherketonetherketoneketone (PEKEKK). In certain embodiments, the PAEK can be PEKK.

[0045] In one embodiment, the poly(aryletherketone) comprises, consists essentially of, or consists of polyetherketoneketone (PEKK). Polyetherketoneketones suitable for use in the present invention may comprise or consist essentially of repeating units represented by the following formulas I and II:

-A-C(=O)-B-C(=O)- I

-A-C(=O)-D-C(=O)- II where A is a p,p'-Ph-O-Ph- group, Ph is a phenylene radical, B is p-phenylene, and D is m- phenylene. The Formula I : Formula II (T:l) isomer ratio in the polyetherketoneketone can range from 100:0 to 0:100. The isomer ratio can be easily varied as can be desired to achieve a certain set of properties, e.g., by varying the relative amounts of the different monomers used to make the polyetherketoneketone.

[0046] Generally speaking, a polyetherketoneketone having a relatively high Formula I :

Formula II ratio will be more crystalline than a polyetherketoneketone having a lower Formula I : Formula II ratio. Thus, the T:l ratio can be adjusted to provide an amorphous (non-crystalline) polyetherketoneketone or a more crystalline polyetherketoneketone, as desired. In one embodiment, a polyetherketoneketone having a T:l isomer ratio of from about 50:50 to about 90:10 can be employed. In some embodiments polyetherketoneketones can have a T:l isomer ratio of from about 55:45 to about 85:15, from about 60:40 to about 80:20, from about 65:35 to about 75:25, about 70:30, or at any ranges between the specified ranges.

[0047] In preferred embodiments, polyetherketoneketones can have a T:l isomer ratio of 50:50 to 78:22. Indeed, these T:l isomer ratios enable to maximize the char yield and minimize the precursor part deformation for the pyrolyzed part. In some embodiments, the polyetherketoneketones can have a T:l isomer ratio of about 55:45 to about 65:35, notably about 60:40. In some other embodiments, the polyetherketoneketones can have a T:l isomer ratio of about 65:35 to about 75:25, notably about 70:30.

[0048] Suitable polyetherketoneketones are sold under the brand name KEPSTAN® supplied by Arkema.

[0049] The reinforcing additive of the invention is discrete and notably do not encompass long fibers and continuous fibers or continuous fabrics, that is to say do not encompass fibers having a length of > 20 mm, or in some embodiment fibers having a length of > 15 mm, or of > 10 mm, or of > 5mm. The advantage of using such reinforcing additives to make the precursor part is that it enables to increase the char content of the pyrolyzed part and improves its mechanical properties compared to a comparative part which would be made of only a polyaryletherketone. At the same time, a precursor part comprising a polyaryletherketone (PAEK) and at least one reinforcing additive is much easier to process, notably by a high production rate process, such as injection molding or extrusion, than a precursor part which would be made of a polyaryletherketone (PAEK) with long or continuous fibers.

[0050] In certain embodiments, the reinforcing additive can be one or more of a carbonaceous additive, a chopped fiber, dispersing agents, and an inorganic additive or mixtures thereof. [0051] In certain embodiments, the additive can be present in an amount of from about 0.1% to about 70% by weight of the total composition of the resin. In certain embodiments, the additive can be present in an amount of from about 1% to about 60% by weight of the total composition of the resin. In certain embodiments, the additive can be present in an amount of from about 5% to about 50% by weight of the total composition of the resin of the precursor part after melt processing.

[0052] In certain embodiments, the reinforcing additive can be present in an amount of about 0.1%, 0.5%, 1%, 5%, 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%, or any ranges between the specified values, based on the weight of the total composition of the resin of the precursor part after melt processing.

[0053] In preferred embodiments, the reinforcing additive can be present in an amount of between 20% and 45%, notably of 25% to 40%, based on the weight of the total composition of the resin of the precursor part after melt processing.

[0054] In certain embodiments, the reinforcing additive can be a carbonaceous additive. In certain embodiments, the carbonaceous additive can be one or more of carbon fiber, carbon nanotubes, graphite, graphene, carbon whisker, a fullerene, carbon black, carbon flake, and buckyballs and mixtures thereof. In certain embodiments, the carbonaceous additive can be aligned by shear from the melt processing.

[0055] In certain embodiments, the carbonaceous additive can have a length of from about 0.1mm to 10mm, from about 0.5mm to 9mm, or from about 1mm to 8mm. In certain embodiments, the carbonaceous additive can have a length of about 0.1mm, 0.5mm, 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, and any ranges between the specified values. In certain embodiments, the carbonaceous additive can have a diameter of from about 0.1pm to 10pm, from about 0.5pm to 9pm, or from about 1pm to 8pm. In certain embodiments, the carbonaceous additive can have a diameter of about 0.1pm, 0.5pm, 1pm, 2pm, 3pm, 4pm, 5pm, 6pm, 7pm, 8pm, 9pm, 10pm, and any ranges between the specified values. The length of additive can be measured via optical microscopy before melt compounding. The diameter of additive can be measured via scanning electron microscopy. [0056] In certain embodiments, the reinforcing additive can be a chopped fiber. In certain embodiments, the chopped fiber comprises one or more of carbon, glass, silica, boron, natural fibers, and polymeric fibers and mixtures thereof. In certain embodiments, the natural fibers can be one or more of cellulose, bamboo, hemp, and jute. In certain embodiments, the polymeric fibers can be one or more of polyamide, polyimides, polyaramid, polyurethane, polyester, and polyurethane, and mixtures thereof.

[0057] In certain embodiments, the chopped fiber is a chopped carbon fiber. The one or more carbon fibers can have a fiber length of from about 0.1mm to 10mm, from about 0.5mm to 9mm, or from about 1mm to 8mm. In certain embodiments, the chopped carbon fiber can have a fiber length of about 0.1mm, 0.5mm, 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, and any ranges between the specified values. In certain embodiments, the chopped carbon fiber can have a diameter of from about 0.1pm to 10pm, from about 0.5pm to 9pm, or from about 1pm to 8pm. In certain embodiments, the chopped carbon fiber can have a diameter of about 0.1pm, 0.5pm, 1pm, 2pm, 3pm, 4pm, 5pm, 6pm, 7pm, 8pm, 9pm, 10pm, and any ranges between the specified values. The length of additive can be measured via optical microscopy before melt compounding. The diameter of additive can be measured via scanning electron microscopy.

[0058] One preferred embodiment is directed to chopped carbon fiber at a loading level of 10-45% , or 15-40%, or 20-35% as measured by weight in a PEKK matrix having a T: I ratio of 55:45 to 85:15.

[0059] More preferred embodiments are directed to chopped carbon fiber at a loading level of between 20% and 45%, notably of 25% to 40% as measured by weight in a PEKK matrix having a T:l ratio of 55:45 to 78:22, notably a T:l ratio of about 60:40 or of about 70:30.

[0060] In certain embodiments, the chopped fiber is a chopped glass fiber. The one or more glass fibers can have a fiber length of from about 0.1mm to 10mm, from about 0.5mm to 9mm, or from about 1mm to 8mm. In certain embodiments, the chopped glass fiber can have a fiber length of about 0.1mm, 0.5mm, 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, and any ranges between the specified values. In certain embodiments, the chopped glass fiber can have a diameter of from about 0.1pm to 10pm, from about 0.5pm to 9pm, or from about 1pm to 8pm. In certain embodiments, the chopped glass fiber can have a diameter of about 0.1pm, 0.5pm, 1pm, 2pm, 3pm, 4pm, 5pm, 6pm, 7pm, 8pm, 9pm, 10pm, and any ranges between the specified values. The length of additive can be measured via optical microscopy before melt compounding. The diameter of additive can be measured via scanning electron microscopy.

[0061] One preferred embodiment is directed to chopped glass fiber at a loading level of 10-45% , or 15-40%, or 20-35% as measured by weight in a PEKK matrix having a T: I ratio of 55:45 to 85:15.

[0062] More preferred embodiments are directed to chopped glass fiber at a loading level of between 20% and 45%, notably of 25% to 40% as measured by weight in a PEKK matrix having a T:l ratio of 55:45 to 78:22, notably a T:l ratio of about 60:40 or of about 70:30.

[0063] In certain embodiments, the reinforcing additive can be an inorganic additive. In certain embodiments, the inorganic additive can be one or more of a group IV, V, or VI carbide, silicids, boride, and nitride. In certain embodiments, the inorganic additive can be in powder form. In certain embodiments, the average particle size of the powder can be from about 0.01pm to 500pm, from about 0.1pm to 250pm, from about 1pm to 100pm, or from about 2pm to 50pm. In certain embodiments, the average particle size of the powder can be 0.01pm, 0.1pm, 0.5pm, 1pm, 5pm, 10pm, 15pm, 20pm, 25pm, 30pm, 40pm, 50pm, 75pm, 100pm, 250pm, 500pm, or any ranges between the specified values.

[0064] In certain embodiments, the reinforcing additive can comprise a dispersing agent. By dispersing agent is meant any moiety that improves separation of additives/particles and/or prevents clumping or settling. In certain embodiments, the dispersing agent can be an organosilicate, oganozirconate, organoaluminate, or oraganotitanate. In certain embodiments, dispersing agent can have an average particle size of from about lnm to 500nm, from about 2nm to 250nm, or from 3nm to lOOnm. In certain embodiments, dispersing agent can have an average particle size of about lnm, 2nm, 3nm, 5nm, lOnm, 15nm, 20nm, 25nm, 30nm, 40nm, 50nm, 75nm, lOOnm, 250nm, 500nm, or any ranges between the specified values. Particle size can be determined by scanning electron microscopy of the dispersing agent before melt compounding.

[0065] According to the invention, during the pyrolyzing, a temperature within a chamber increases at a rate of from about l°C/h to about 20°C/h up. Generally, the temperature within the chamber is increased to a peak temperature of about 1000°C. In some cases though, the temperature within the chamber may be increased to a lower temperature of: about 850°C, or about 900°C, or about 950°C.

[0066] In certain embodiments, during the pyrolyzing the temperature within the chamber can increase at a rate of from about 3°C/h to about 17°C/h. In certain embodiments, during the pyrolyzing, the temperature within the chamber can increase at a rate of from about 5°C/h to about 15°C/h. In certain embodiments, pyrolysis conditions during pyrolyzing step b. are the same as the pyrolysis conditions during pyrolyzing step d. In certain embodiments, the pyrolysis conditions during pyrolyzing step b. are different than the pyrolysis conditions during pyrolyzing step d.

[0067] In certain embodiments, during the pyrolyzing, a temperature within a chamber can increase at a rate of from about l°C/h, 2°C/h, 3°C/h, 4°C/h, 5°C/h, 6°C/h, 7°C/h, 8°C/h, 9°C/h, 10°C/h, ll ^o C/h, 12°C/h, 13°C/h, 14°C/h, 15°C/h, 16°C/h, 17°C/h, 18°C/h, 19°C/h, 20°C/h, or any ranges between the specified values.

[0068] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature below 450°C, or at a temperature below 400°C.

[0069] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature above 600°C, or at a temperature above 650°C or more.

[0070] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of less than 10 °C/h between 400°C and 650°C, or between 450°C and 600 °C. In particular, the temperature within the chamber can increase at a rate of from about l°C/h, 2°C/h, 3°C/h, 4°C/h, 5°C/h, 6°C/h, 7°C/h, 8°C/h, 9°C/h, 10°C/h between 400°C and 650°C, or from 450°C and 600°C. [0071] In preferred embodiments, during the pyrolyzing of the precursor part the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature below 400°C, at a rate of less than 10 °C/h between 450°C and 600 °C, and at a rate of 10 °C/h or more at a temperature above 650°C.

[0072] In certain embodiments, during the pyrolyzing of the precursor part the temperature within the chamber increases one or more times at a rate of from 10 °C/h to 15°C/h at a temperature below 400°C, at a rate of from 2°C/h to 5 °C/h between 450°C and 600 °C, and at a rate of from 10 °C/h to 15°C/h at a temperature above 650°C.

[0073] In certain embodiments, the pyrolyzing optionally can comprise temperature holds during the pyrolysis at temperatures between 120 °C and 1000 °C, or between 200°C and 1000°C, or between 400°C and 1000°C. In certain embodiments, the pyrolysis can be performed under nitrogen, argon, or forming gas (mixture of hydrogen and nitrogen). In certain embodiments, the pyrolyzing occurs in a graphite bed. In certain embodiments, the temperature holds during the pyrolysis can be from about lh to 72h, from about 2h to 48h, orfrom about 3h to 24h. In certain embodiments, the temperature holds (i.e., is maintained) during the pyrolysis can be about lh, 2h, 3h, 4h, 5h, 6h, 7h, 8h, 9h, lOh, 12h, 16h, 20h, 24h, 30h, 36h, 42h, 48h, 54h, 60h, 66h, 72h, or any ranges between the specified values.

[0074] In certain embodiments, the pyrolyzing of the precursor part can comprise one or more temperature holds during the pyrolysis between 400°C and 650°C, or between 450°C and 600°C, temperatures included. In certain embodiments, the pyrolysis of the precursor part can be performed under nitrogen, argon, or forming gas (mixture of hydrogen and nitrogen). In certain embodiments, the pyrolyzing of the precursor part occurs in a graphite bed. In certain embodiments, the temperature holds during the pyrolysis can be from about lh to 72h, from about 2h to 48h, or from about 3h to 24h. In certain embodiments, the temperature holds (i.e., is maintained) during the pyrolysis of the precursor part can be about lh, 2h, 3h, 4h, 5h, 6h, 7h, 8h, 9h, lOh, 12h, 16h, 20h, 24h, 30h, 36h, 42h, 48h, 54h, 60h, 66h, 72h, or any ranges between the specified values.

[0075] In certain embodiments, the liquid second resin comprises, consists essentially of, or consists of one or more of pitch, benzoxazines, furfural, polyester, vinylester, acrylic, and phenolics. In certain embodiment, the liquid second resin comprises, consists essentially of, or consist of pitch, phenolics or combination thereof.

[0076] In certain embodiments, the method comprises repeating infusing step c. and pyrolyzing step d. at least one time. In certain embodiments, the method comprises repeating infusing step c. and pyrolyzing step d. at least two, three, four, five, or more times. In certain embodiments the char yield after a first pyrolysis cycle or after two, three, four, five, or more times can be greater than 65%, greater than 70%, greater than 75%, greater than 80%, greater than 85%, greater than 90%, or greater than 95% or more.

[0077] In certain embodiments, the method comprises repeating infusing step c. and pyrolyzing step d. until the carbon carbon composite, carbon ceramic matrix composite, or carbon silica composite is at least about 75% solid, 80% solid, 85% solid, 90% solid, 95% solid, or 99% solid as determined according to Example 1.

[0078] In certain embodiments, the method comprises repeating steps c. through d. one or more times.

Method comprising aligned additives

[0079] In certain embodiments, the present disclosure is directed to a method for preparing a carbon-carbon composite, a carbon ceramic matrix composite, or a carbon silica composite.

[0080] In certain embodiments, the method for preparing a carbon-carbon composite, a carbon ceramic matrix composite, or a carbon silica composite comprises: al) processing aligned reinforcing additives and a resin comprising a polyaryletherketone (PAEK) to make an aligned reinforcing additives PAEK, aligned 1-2 dimensional flake material, or aligned 1-2 dimensional platelet material, to create a fabric, prepreg, or tape comprising the aligned reinforcing additives and impregnated PAEK, a2) processing the PAEK tape, prepreg, or fabric via hand-layup, automated tape placement, 3D printing, r filament winding, or needle punching or other methods of Z-axis reinforcement followed by compression molding, vacuum bag consolidation, autoclave consolidation, in-situ consolidation to make a precursor object, c. pyrolyzing the object to make a pyrolyzed object, d. infusing a liquid second resin into the pyrolyzed object to make an infused object, and e. pyrolyzing the infused object to make the carbon carbon composite, the carbon ceramic matrix composite, or the carbon silica composite, and f. optionally repeating steps c. through d. one or more times.

[0081] In certain embodiments, the present disclosure is directed to the carbon carbon composite, carbon ceramic matrix composite, or carbon silica composite made by the method above.

[0082] In certain embodiments, the method comprises processing aligned reinforcing additives and a resin comprising a polyaryletherketone (PAEK) to make an aligned reinforcing additives PAEK. In certain embodiments, the method comprises processing aligned reinforcing additives and a resin comprising a polyaryletherketone (PAEK) to make an aligned 1-2 dimensional flake material. In certain embodiments, the method comprises processing aligned reinforcing additives and a resin comprising a polyaryletherketone (PAEK) to make an aligned 1-2 dimensional platelet material. In certain embodiments, the aligned 1-2 dimensional flake material or aligned 1-2 dimensional platelet material can be graphite, graphene, or whiskers.

[0083] In certain embodiments, the 1-2 dimensional flake material or 1-2 dimensional platelet material can have a diameter of from about 0.1mm to 10mm, from about 0.5mm to 9mm, or from about 1mm to 8mm. In certain embodiments, the 1-2 dimensional flake material or 1-2 dimensional platelet material can have a diameter of about 0.1mm, 0.5mm, 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, and any ranges between the specified values. In certain embodiments, the 1-2 dimensional flake material or 1-2 dimensional platelet material can have a thickness of from about 0.001mm to 0.1mm, from about 0.005mm to 0.09mm, or from about 0.01mm to 0.08mm. In certain embodiments, the 1-2 dimensional flake material or 1-2 dimensional platelet material can have a thickness of about 0.001mm, 0.005mm, 0.01mm, 0.02mm, 0.03mm, 0.04mm, 0.05mm, 0.06mm, 0.07mm, 0.08mm, 0.09mm, 0.1mm, and any ranges between the specified values. Measurements can be obtained from optical or scanning electron microscopy imaging before melt compounding.

[0084] In certain embodiments, the processing can create a fabric comprising the aligned reinforcing additives and impregnated PAEK. In certain embodiments, the processing can create a prepreg comprising the aligned reinforcing additives and impregnated PAEK. In certain embodiments, the processing can create a tape comprising the aligned reinforcing additives and impregnated PAEK.

[0085] In certain embodiments, the aligned reinforcing additives can be made by stretching unidirectional tape until the fibers are broken, subjecting the fibers to fluid flow to align the fibers, or subjecting the fibers to electro-magnetic fields to align the fibers. In certain embodiments, the aligned reinforcing additives can be made by stretching unidirectional tape until the fibers are broken (either before or after impregnation with PAEK resin). In a preferred embodiment the fibers are aligned by fluid flow onto a porous belt to create a mat of aligned fibers as described in U.S. 10,669,659.

[0086] In certain embodiments, the aligned reinforcing additives can be one or more of carbon, glass, silica, boron, natural fibers, polymeric fibers, carbon nanotubes, graphite, graphene, and carbon or ceramic whiskers. In certain embodiments, the natural fibers can be one or more of cellulose, bamboo, hemp, and jute. In certain embodiments, the polymeric fibers can be one or more of polyamide, polyimides, polyaramid, polyurethane, polyester, and polyurethane.

[0087] In certain embodiments, the aligned reinforcing additive can have a length of from about 0.1mm to 10mm, from about 0.5mm to 9mm, or from about 1mm to 8mm. In certain embodiments, the aligned reinforcing additive can have a fiber length of about 0.1mm, 0.5mm, 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, and any ranges between the specified values.

[0088] In certain embodiments, the PAEK can be one or more of polyetherketoneketone (PEKK), polyetheretherketone (PEEK), polyetheretherketone-polyfether diphenyl ether ketone) (PEEK-PEDEK), polyetherketone (PEK), polyetherketone (PEK), and polyetherketonetherketoneketone (PEKEKK). In certain embodiments, the PAEK can be PEKK. In some embodiments, PEKK is preferred. In other embodiments PEEK is preferred.

[0089] In one embodiment, the poly(aryletherketone) comprises, consists essentially of, or consists of polyetherketoneketone (PEKK). Polyetherketoneketones suitable for use in the present invention may comprise or consist essentially of repeating units represented by the following formulas I and II:

-A-C(=O)-B-C(=O)- I

-A-C(=O)-D-C(=O)- II where A is a p,p'-Ph-O-Ph- group, Ph is a phenylene radical, B is p-phenylene, and D is m- phenylene. The Formula I : Formula II (T:l) isomer ratio in the polyetherketoneketone can range from 100:0 to 0:100. The isomer ratio can be easily varied as can be desired to achieve a certain set of properties, e.g., by varying the relative amounts of the different monomers used to make the polyetherketoneketone.

[0090] Generally speaking, a polyetherketoneketone having a relatively high Formula I : Formula II ratio will be more crystalline than a polyetherketoneketone having a lower Formula I : Formula II ratio. Thus, the T:l ratio can be adjusted to provide an amorphous (non-crystalline) polyetherketoneketone or a more crystalline polyetherketoneketone, as desired. In one embodiment, a polyetherketoneketone having a T:l isomer ratio of from about 50:50 to about 90:10 can be employed. In some embodiments polyetherketoneketones can have a T:l isomer ratio of from about 55:45 to about 85:15, from about 60:40 to about 80:20, from about 65:35 to about 75:25, about 70:30, or at any ranges between the specified ranges.

[0091] In preferred embodiments, polyetherketoneketones can have a T:l isomer ratio of 50:50 to 78:22. In some embodiments, the polyetherketoneketones can have a T:l isomer ratio of about 55:45 to about 65:35, notably about 60:40. In some other embodiments, the polyetherketoneketones can have a T:l isomer ratio of about 65:35 to about 75:25, notably about 70:30.

[0092] In certain embodiments, the in-situ consolidation can contain rolling to apply pressure and/or heat. [0093] In certain embodiments, during the pyrolyzing, a temperature within a chamber can increase at a rate of from about l°C/h to about 20°C/h up to a peak temperature of about 1000°C. In certain embodiments, during the pyrolyzing, the temperature within the chamber can increase at a rate of from about 3°C/h to about 17°C/h. In certain embodiments, during the pyrolyzing, the temperature within the chamber can increase at a rate of from about 5°C/h to about 15°C/h. In certain embodiments, the pyrolysis conditions during pyrolyzing step c. are the same as the pyrolysis conditions during pyrolyzing step e. In certain embodiments, the pyrolysis conditions during pyrolyzing step c. are different than the pyrolysis conditions during pyrolyzing step e.

[0094] In certain embodiments, during the pyrolyzing, a temperature within a chamber can increase at a rate of from about l°C/h, 2°C/h, 3°C/h, 4°C/h, 5°C/h, 6°C/h, 7°C/h, 8°C/h, 9°C/h, 10°C/h, ll ^o C/h, 12°C/h, 13°C/h, 14°C/h, 15°C/h, 16°C/h, 17°C/h, 18°C/h, 19°C/h, 20°C/h, or any ranges between the specified values.

[0095] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature below 450°C, or at a temperature below 400°C.

[0096] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature above 600°C, or at a temperature above 650°C or more.

[0097] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of less than 10 °C/h between 400°C and 650°C, or between 450°C and 600 °C. In particular the temperature within the chamber can increase at a rate of from about l°C/h, 2°C/h, 3°C/h, 4°C/h, 5°C/h, 6°C/h, 7°C/h, 8°C/h, 9°C/h, 10°C/h between 400°C and 650°C, or from 450°C and 600°C.

[0098] In preferred embodiments, during the pyrolyzing of the precursor part the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature below 400°C, at a rate of less than 10 °C/h between 450°C and 600 °C, and at a rate of 10 °C/h or more at a temperature above 650°C. [0099] In certain embodiments, during the pyrolyzing of the precursor part the temperature within the chamber increases one or more times at a rate of from 10 °C/h to 15°C/h at a temperature below 400°C, at a rate of from 2°C/h to 5 °C/h between 450°C and 600 °C, and at a rate of from 10 °C/h to 15°C/h at a temperature above 650°C.

[0100] In certain embodiments, the pyrolyzing optionally can comprise temperature holds during the pyrolysis. In certain embodiments, the pyrolysis can be performed under nitrogen, argon, or forming gas. In certain embodiments, the pyrolyzing occurs in a graphite bed. In certain embodiments, the temperature holds during the pyrolysis can be from about lh to 72h, from about 2h to 48h, or from about 3h to 24h. In certain embodiments, the temperature holds during the pyrolysis can be about lh, 2h, 3h, 4h, 5h, 6h, 7h, 8h, 9h, lOh, 12h, 16h, 20h, 24h, 30h, 36h, 42h, 48h, 54h, 60h, 66h, 72h, or any ranges between the specified values.

[0101] In certain embodiments, the pyrolyzing of the precursor part can comprise one or more temperature holds during the pyrolysis between 400°C and 650°C, or between 450°C and 600°C, temperatures included. In certain embodiments, the pyrolysis of the precursor part can be performed under nitrogen, argon, or forming gas (mixture of hydrogen and nitrogen). In certain embodiments, the pyrolyzing of the precursor part occurs in a graphite bed. In certain embodiments, the temperature holds during the pyrolysis can be from about lh to 72h, from about 2h to 48h, or from about 3h to 24h. In certain embodiments, the temperature holds (i.e., is maintained) during the pyrolysis of the precursor part can be about lh, 2h, 3h, 4h, 5h, 6h, 7h, 8h, 9h, lOh, 12h, 16h, 20h, 24h, 30h, 36h, 42h, 48h, 54h, 60h, 66h, 72h, or any ranges between the specified values.

[0102] In certain embodiments, the precursor object can be melt formed after the processing step a. but before the pyrolyzing step c.

[0103] In certain embodiments, the liquid second resin can be one or more of pitch, benzoxazines, furfural, polyester, vinylester, acrylic, and phenolics. In certain embodiments, pitch, phenolics, or combination there are preferred.

[0104] In certain embodiments, the method comprises repeating infusing step d. and pyrolyzing step e. at least one time. In certain embodiments, the method comprises repeating infusing step d. and pyrolyzing step e. at least two, three, four, or five times. In certain embodiments the char yield after a first pyrolysis cycle or after two, three, four, five, or more times can be greater than 65%, greater than 70%, greater than 75%, greater than 80%, greater than 85%, greater than 90%, or greater than 95% or more.

[0105] In certain embodiments, the method comprises repeating infusing step d. and pyrolyzing step e. until the carbon carbon composite, carbon ceramic matrix composite, or carbon silica composite is at least about 75% solid, 80% solid, 85% solid, 90% solid, 95% solid, or 99% solid.

[0106] In certain embodiments, steps c. through d. are repeated one or more times.

Method comprising impregnating or co-weaving

[0107] In certain embodiments, the present disclosure is directed to a method for making a carbon-carbon composite, a carbon ceramic matrix composite, or a carbon silica composite.

[0108] In certain embodiments, the method for making a carbon carbon composite, a carbon ceramic matrix composite, or a carbon silica composite comprises: al) impregnating a continuous fiber tape or fabric with a resin comprising a polyaryletherketone (PAEK) and at least one reinforcing additive to make a filled PAEK tape or fabric or co-weaving a continuous fiber or fabric with a PAEK fiber comprising PAEK and the at least one reinforcing additive to make a filled PAEK tape or fabric, a2) processing the filled PAEK tape or fabric or co-woven PAEK/fiber material via handlayup, automated tape placement, 3D printing, filament winding or needle punching or other methods of Z-axis reinforcement followed by compression molding, vacuum bag consolidation, autoclave consolidation, or in-situ consolidation to make a precursor part, c. pyrolyzing the precursor part to make a pyrolyzed part, d. infusing a liquid second resin into the pyrolyzed part to make an infused part, and e. pyrolyzing the infused part to make the carbon carbon composite, the carbon ceramic matrix composite, or the carbon silica composite. [0109] In certain embodiments, the present disclosure is directed to the carbon carbon composite, carbon ceramic matrix composite, or carbon silica composite made by the method above.

[0110] In certain embodiments, the method comprises impregnating a continuous fiber tape or fabric with a resin comprising a polyaryletherketone (PAEK) and at least one additive to make a filled PAEK tape. In certain embodiments, the method comprises co-weaving a continuous fiber or fabric with a PAEK fiber comprising PAEK and at least one additive to make a filled PAEK tape or fabric.

[0111] In certain embodiments, the continuous fiber or fabric can be carbon fiber.

[0112] In certain embodiments, the PAEK can be one or more of polyetherketoneketone

(PEKK), polyetheretherketone (PEEK), polyetheretherketone-polyfether diphenyl ether ketone) (PEEK-PEDEK), polyetherketone (PEK) and polyetherketonetherketoneketone (PEKEKK). In certain embodiments, the PAEK can be PEKK.

[0113] In one embodiment, the poly(aryletherketone) comprises, consists essentially of, or consists of polyetherketoneketone (PEKK). Polyetherketoneketones suitable for use in the present invention may comprise or consist essentially of repeating units represented by the following formulas I and II:

-A-C(=O)-B-C(=O)- I

-A-C(=O)-D-C(=O)- II where A is a p,p'-Ph-O-Ph- group, Ph is a phenylene radical, B is p-phenylene, and D is m- phenylene. The Formula I : Formula II (T:l) isomer ratio in the polyetherketoneketone can range from 100:0 to 0:100. The isomer ratio can be easily varied as can be desired to achieve a certain set of properties, e.g., by varying the relative amounts of the different monomers used to make the polyetherketoneketone.

[0114] Generally speaking, a polyetherketoneketone having a relatively high Formula I : Formula II ratio will be more crystalline than a polyetherketoneketone having a lower Formula I : Formula II ratio. Thus, the T:l ratio can be adjusted to provide an amorphous (non-crystalline) polyetherketoneketone or a more crystalline polyetherketoneketone, as desired. In one embodiment, a polyetherketoneketone having a T:l isomer ratio of from about 50:50 to about 90:10 can be employed. In some embodiments polyetherketoneketones can have a T:l isomer ratio of from about 55:45 to about 85:15, from about 60:40 to about 80:20, from about 65:35 to about 75:25, about 70:30, or at any ranges between the specified ranges.

[0115] In preferred embodiments, polyetherketoneketones can have a T:l isomer ratio of 50:50 to 78:22. Indeed, these T:l isomer ratios enable to maximize the char yield and minimize the precursor part deformation for the pyrolyzed part. In some embodiments, the polyetherketoneketones can have a T:l isomer ratio of about 55:45 to about 65:35, notably about 60:40. In some other embodiments, the polyetherketoneketones can have a T:l isomer ratio of about 65:35 to about 75:25, notably about 70:30.

[0116] In certain embodiments, the reinforcing additive can be one or more of a carbonaceous additive, a chopped fiber, dispersing agents, and an inorganic additive.

[0117] In certain embodiments, the additive can be present in an amount of from about 0.01% to about 30% by weight of the total composition of the resin. In certain embodiments, the additive can be present in an amount of from about 0.1% to about 25% by weight of the total composition of the resin. In certain embodiments, the additive can be present in an amount of from about 1% to about 20% by weight of the total composition of the resin.

[0118] In certain embodiments, the additive can be present in an amount of about 0.01%, 0.05%, 0.1%, 0.5%, 1%, 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9%, 10%, 15%, 20%, 25%, 30%, or any ranges between the specified values, based on the weight of the total composition of the resin.

[0119] In certain embodiments, the additive can be a carbonaceous additive. In certain embodiments, the carbonaceous additive can be one or more of carbon fiber, carbon nanotubes, graphite, graphene, carbon whisker, a fullerene, carbon black, carbon flake, and buckyballs. In certain embodiments, the carbonaceous additive can be aligned by shear from the melt processing.

[0120] In certain embodiments, the carbonaceous additive can have a length of from about 0.1mm to 10mm, from about 0.5mm to 9mm, or from about 1mm to 8mm. In certain embodiments, the carbonaceous additive can have a length of about 0.1mm, 0.5mm, 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, and any ranges between the specified values. In certain embodiments, the carbonaceous additive can have a diameter of from about 0.1pm to 10pm, from about 0.5pm to 9pm, or from about 1pm to 8pm. In certain embodiments, the carbonaceous additive can have a diameter of about 0.1pm, 0.5pm, 1pm, 2pm, 3pm, 4pm, 5pm, 6pm, 7pm, 8pm, 9pm, 10pm, and any ranges between the specified values.

[0121] In certain embodiments, the additive can be a chopped fiber. In certain embodiments, the chopped fiber comprises one or more of carbon, glass, silica, boron, natural fibers, and polymeric fibers. In certain embodiments, the natural fibers can be one or more of cellulose, bamboo, hemp, and jute. In certain embodiments, the polymeric fibers can be one or more of polyamide, polyimides, polyaramid, polyurethane, polyester, and polyurethane.

[0122] In certain embodiments, the chopped fiber is a chopped carbon fiber. The one or more carbon fibers can have a fiber length of from about 0.1mm to 10mm, from about 0.5mm to 9mm, or from about 1mm to 8mm. In certain embodiments, the chopped carbon fiber can have a fiber length of about 0.1mm, 0.5mm, 1mm, 2mm, 3mm, 4mm, 5mm, 6mm, 7mm, 8mm, 9mm, 10mm, and any ranges between the specified values. In certain embodiments, the chopped carbon fiber can have a diameter of from about 0.1pm to 10pm, from about 0.5pm to 9pm, or from about 1pm to 8pm. In certain embodiments, the chopped carbon fiber can have a diameter of about 0.1pm, 0.5pm, 1pm, 2pm, 3pm, 4pm, 5pm, 6pm, 7pm, 8pm, 9pm, 10pm, and any ranges between the specified values.

[0123] In certain embodiments, the additive can be an inorganic additive. In certain embodiments, the inorganic additive can be one or more of a group IV, V, or VI carbide, silicides, boride, and nitride. Carbides and silicides would be preferred with silicon carbide being the most preferred. In certain embodiments, the inorganic additive can be in powder form. In certain embodiments, the average particle size of the powder can be from about 0.01pm to 500pm, from about 0.1pm to 250pm, from about 1pm to 100pm, or from about 2pm to 50pm. In certain embodiments, the average particle size of the powder can be 0.01pm, 0.1pm, 0.5p.m lpm, 5pm, 10pm, 15pm, 20pm, 25pm, 30pm, 40pm, 50pm, 75pm, 100pm, 250|u.m, 500pm, or any ranges between the specified values.

[0124] In certain embodiments, the additive can comprise a dispersing agent. In certain embodiments, the dispersing agent can be an organosilicate, oganozirconate, organoaluminate, or oraganotitanate, with organosilicates and organotitanates being preffered and organosilicates being the most preferred. In certain embodiments, dispersing agent can have an average pore size of from about lnm to 500nm, from about 2nm to 250nm, or from 3nm to lOOnm. In certain embodiments, dispersing agent can have an average pore size of about lnm, 2nm, 3nm, 5nm, lOnm, 15nm, 20nm, 25nm, 30nm, 40nm, 50nm, 75nm, lOOnm, 250nm, 500nm, or any ranges between the specified values.

[0125] In certain embodiments, the in-situ consolidation can contain rolling to apply pressure and/or heat.

[0126] In certain embodiments, during the pyrolyzing, a temperature within a chamber can increase at a rate of from about l°C/h to about 20°C/h up to a peak temperature of about 1000°C. In certain embodiments, during the pyrolyzing, the temperature within the chamber can increase at a rate of from about 3°C/h to about 17°C/h. In certain embodiments, during the pyrolyzing, the temperature within the chamber can increase at a rate of from about 5°C/h to about 15°C/h. In certain embodiments, the pyrolysis conditions during pyrolyzing step c. are the same as the pyrolysis conditions during pyrolyzing step e. In certain embodiments, the pyrolysis conditions during pyrolyzing step c. are different than the pyrolysis conditions during pyrolyzing step e.

[0127] In certain embodiments, during the pyrolyzing, a temperature within a chamber can increases at a rate of from about l°C/h, 2°C/h, 3°C/h, 4°C/h, 5°C/h, 6°C/h, 7°C/h, 8°C/h, 9°C/h, 10°C/h, ll ^o C/h, 12°C/h, 13°C/h, 14°C/h, 15°C/h, 16°C/h, 17°C/h, 18°C/h, 19°C/h, 20°C/h, or any ranges between the specified values.

[0128] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature below 450°C, or at a temperature below 400°C. [0129] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature above 600°C, or at a temperature above 650°C or more.

[0130] In certain embodiments, during the pyrolyzing of the precursor part, the temperature within the chamber increases one or more times at a rate of less than 10 °C/h between 400°C and 650°C, or between 450°C and 600 °C . In particular the temperature within the chamber can increase at a rate of from about l°C/h, 2°C/h, 3°C/h, 4°C/h, 5°C/h, 6°C/h, 7°C/h, 8°C/h, 9°C/h, 10°C/h between 400°C and 650°C, or from 450°C and 600°C.

[0131] In preferred embodiments, during the pyrolyzing of the precursor part the temperature within the chamber increases one or more times at a rate of 10 °C/h or more at a temperature below 400°C, at a rate of less than 10 °C/h between 450°C and 600 °C, and at a rate of 10 °C/h or more at a temperature above 650°C.

[0132] In certain embodiments, during the pyrolyzing of the precursor part the temperature within the chamber increases one or more times at a rate of from 10 °C/h to 15°C/h at a temperature below 400°C, at a rate of from 2°C/h to 5 °C/h between 450°C and 600 °C, and at a rate of from 10 °C/h to 15°C/h at a temperature above 650°C.

[0133] In certain embodiments, the pyrolyzing optionally can comprise temperature holds during the pyrolysis. In certain embodiments, the pyrolysis can be performed under nitrogen, argon, or forming gas. In certain embodiments, the pyrolyzing occurs in a graphite bed. In certain embodiments, the temperature holds during the pyrolysis can be from about lh to 72h, from about 2h to 48h, or from about 3h to 24h. In certain embodiments, the temperature holds during the pyrolysis can be about lh, 2h, 3h, 4h, 5h, 6h, 7h, 8h, 9h, lOh, 12h, 16h, 20h, 24h, 30h, 36h, 42h, 48h, 54h, 60h, 66h, 72h, or any ranges between the specified values.

[0134] In certain embodiments, the pyrolyzing of the precursor part can comprise one or more temperature holds during the pyrolysis between 450°C and 600°C, temperatures included. In certain embodiments, the pyrolysis of the precursor part can be performed under nitrogen, argon, or forming gas (mixture of hydrogen and nitrogen). In certain embodiments, the pyrolyzing of the precursor part occurs in a graphite bed. In certain embodiments, the temperature holds during the pyrolysis can be from about lh to 72h, from about 2h to 48h, or from about 3h to 24h. In certain embodiments, the temperature holds (i.e., is maintained) during the pyrolysis of the precursor part can be about lh, 2h, 3h, 4h, 5h, 6h, 7h, 8h, 9h, lOh, 12h, 16h, 20h, 24h, 30h, 36h, 42h, 48h, 54h, 60h, 66h, 72h, or any ranges between the specified values.

[0135] In certain embodiments, the precursor object can be melt formed after the processing step b. but before the pyrolyzing step c.

[0136] In certain embodiments, the liquid second resin can be one or more of pitch, benzoxazines, furfural, polyester, vinylester, acrylic, and phenolics.

[0137] In certain embodiments, the method comprises repeating infusing step d. and pyrolyzing step e. at least one time. In certain embodiments, the method comprises repeating infusing step d. and pyrolyzing step e. at least two, three, four, or five times or more. In certain embodiments the char yield after a first pyrolysis cycle or after two, three, four, five, or more times can be greater than 65%, greater than 70%, greater than 75%, greater than 80%, greater than 85%, greater than 90%, or greater than 95% or more.

[0138] In certain embodiments, the method comprises repeating infusing step d. and pyrolyzing step e. until the carbon carbon composite, carbon ceramic matrix composite, or carbon silica composite is at least about 75% solid, 80% solid, 85% solid, 90% solid, 95% solid, or 99% solid.

EXAMPLES

[0139] The method and products described herein are now further detailed with reference to the following examples. These examples are provided for the purpose of illustration only and the embodiments described herein should in no way be construed as being limited to these examples. Rather, the embodiments should be construed to encompass any and all variations which become evident as a result of the teaching provided herein.

[0140] Example nb 1: Pyrolysis of 0-40% Carbon-Filled PAEK Resin

Several variations of the proposed invention were evaluated for char yield. Injection molded Tensile bars comprising neat resin (with varying T/l content from 60/40 to 80/20) and short strand chopped carbon fiber (0-40%) were analyzed ("Table 1"). The tensile bars consisting only of PEKK represented comparative examples, while the example with 40% chopped carbon fiber is of the invention.

[0141]

Table 1

[0142] All samples underwent the following pyrolysis cycle under an inert atmosphere

(Nitrogen flowing at 10-15 LPM throughout) ("Table 2"):

[0143]

Table 2

[0144] Char yield was calculated from the mass of each sample pre and post pyrolysis

("Equation 1"): ^vv a char yield (%) = — X 100 w _b where Wb and w _a are the mass of the sample before and after pyrolysis respectively.

Results are summarized below ("Table 3"). It can be seen that example E, shown in Figure 1, which contains carbon fiber fillers and is of the invention, had significantly higher char yield than COMPARATIVE Examples A-D.

[0145]

Table 3

[0146] Example nb 2 : Influence of T/l ratio for PEKK samples

PEKK samples with varying T/l ratios (60/40 ; 80/20) and 30% chopped fibers (either glass or carbon) ("Table 4") were fabricated by injection molded and pyrolyzed in a quartz crucible in a muffle furnace in an inert environment undergoing the following pyrolysis cycle ("Table 5"). Their initial dimensions were all around: 5,1 cm x 1,3 cm x 0,3 cm.

[0147]

Table 4 [0148]

Table 5

[0149] Samples F and G were weighed and their thickness (t) was measured before and after pyrolysis to calculate char yield and determine dimensional change ("Table 6").

The parameter At refers to the difference between the thickness after the pyrolysis and the thickness, at 25°C before the pyrolysis, divided by the thickness, at 25°C before the pyrolysis, expressed as a percentage.

[0150] Table 6

[0151] Example F (T:l ratio of 60:40) exhibited a slight improvement in char yield when compared to example G (T: I ratio of 80:20). More significantly, Example F showed an almost 3x reduction in sample bloating, as measured by dimensional changes in thickness, when compared to Example G.

[0152] Example nb 3 : Influence of the temperature increase profile during pyrolyzing

Samples of polyetherketoneketone (PEKK) with varying T/l ratios (60/40, 70/30, 80/20) and polyetheretherketone (PEEK; homopolymer consisting of repeating unit of formula (III)) with varying short strand chopped carbon fiber content (0-40 wt%) were fabricated by injection molding and pyrolyzed in a quartz crucible in a muffle furnace with slow ramp rates (undergoing the pyrolysis cycle of Table 5) and extended holds up to 1000°C in an inert environment.

As a comparison, a fast ramp rate (set to 20°C/min) was used with a hold at 1000°C for 3 hours in an inert environment to pyrolyze comparative samples fabricated the same way. Although the furnace was set to a fast ramp rate, the furnace did not fully operate at this fast of a rate and was estimated to run closer to l-5°C/min. Samples were weighed and their thickness was measured before and after pyrolysis to calculate char yield and determine dimensional changes.

[0153]

It was observed for all comparable samples, that a fast ramp for pyrolyzing causes significant higher dimensional changes as compared to a slow ramp, and comparable or slightly higher char yield. In addition, neat PEEK appeared to have significant lower char yield than neat PEKK in the same pyrolysis conditions.