Method for producing sized, coated ceramic fibers

Abstract: The present invention provides a method for producing sized ceramic fibers, such as silicon carbide and silicon oxycarbide, by coating with an acrylate-based non-aqueous sizing composition. The fibers may also be coated with interfacial coatings. Some interfacial coatings are moisture-reactive. The sizing protects the fiber and interfacial coatings from moisture and mechanical damage during winding and weaving. The sizing can subsequently be removed in an inert environment at low temperature.

Description: This invention provides a method for producing a sized, coated ceramic fiber, using a specific sizing composition which makes the fiber easier to handle, wind and weave. Ceramic composite materials used in high temperature applications require the use of a ceramic fiber for reinforcement. Commercially available ceramic fibers are typically provided with a sizing on the fiber. Generally, any sizing is removed before coating the ceramic fiber with an interfacial coating. The resulting fiber is difficult to handle, filament wind or weave into a 2-dimensional fabric or 3-dimensional pre-form. Additionally, an unsized fiber is prone to mechanical damage. U.S. Patent 5,093,155 discloses a sizing liquid containing a sulfone compound and a solvent such as water or an organic solvent. The sizing is applied to fibers, including carbon, boron, ceramic and metal fibers. The fibers are then incorporated into a matrix resin to make a composite. The sizing enhances adhesion between the fibers and the matrix. U.S. Patent 5,130,194 describes a coating for ceramic fibers used in composites. The fibers therein are generally coated with a silanol and a difunctional organic coupling agent in a water or alcohol solvent. The silanol provides hydroxyl groups on the fiber and the coupling agent connects the hydroxyl binding sites to a resin to form a composite. However, aqueous sizing materials can damage coated fibers if the coating is moisture sensitive, resulting in deteriorated composite properties. U.S. Patent 5,173,367 claims a fiber reinforced ceramic composite. The fiber has a 2 layer size obtained by sizing the fibers with a solution of an organic solvent, a metal oxide and a titanium compound. The fibers are then sized with an organic solvent solution of a polycarbosilane or polysilazane. The sizing protects the fibers from oxidative deterioration. An object of the present invention is to provide a non-aqueous sizing for ceramic fibers that makes the fibers easier to handle, wind and weave. Another object of our invention is to provide a sizing that is easily removed by heat treatment at low temperature and which leaves little or no residue when decomposed in an inert atmosphere. A final object of this invention is to produce a sized fiber that is less prone to moisture and mechanical damage. The present invention introduces a non-aqueous sizing composition for ceramic fibers, wherein the ceramic fibers having interfacial coatings. The sizing composition used in the method according to the present invention comprises both a sizing compound and a curing agent. Suitable sizing compounds for use herein are multifunctional acrylates or multifunctional methacrylates. Multifunctional acrylates have at least two acrylate groups per molecule. Multifunctional methacrylates have at least two methacrylate groups per molecule. The sizing compound can be either a monomer or a polymer. The amount of the sizing compound in our non-aqueous sizing composition is typically 1 to 98%, preferably 12 to 38%, by weight of the non-aqueous sizing composition. Suitable multifunctional acrylates and multifunctional methacrylates for the claimed sizing compound are exemplified by those disclosed in U.S. Patent 5,626,964 which provides further details and examples of multifunctional acrylates and multifunctional methacrylates. Suitable multifunctional acrylate monomers include diacrylates, triacrylates, tetraacrylates and pentaacrylates. Suitable diacrylates include: 1,6-hexanediol diacrylate, 1,4-butanediol diacrylate, ethylene glycol diacrylate, diethylene glycol diacrylate, tetraethylene glycol diacrylate, tripropylene glycol diacrylate, neopentyl glycol diacrylate, poly(butanediol) diacrylate, 1,3-butylene glycol diacrylate, triethylene glycol diacrylate, triisopryopylene glycol diacrylate and polyethylene glycol diacrylate. Examples of suitable triacrylates include trimethylolpropane triacrylate, trimethylolpropane triethoxy triacrylate and pentaerythritol monohydroxy triacrylate. Trimethylol propane triacrylate is preferred when the sizing compound is a multifunctional acrylate monomer. Examples of suitable tetraacrylates include pentaerythritol tetraacrylate and di-trimethylolpropane tetraacrylate. Suitable pentaacrylates include dipentaerythritol (monohydroxy) pentacrylate. Suitable multifunctional methacrylate monomers include dimethacrylates, trimethacrylates, tetramethacrylates and pentamethacrylates. Examples of suitable dimethacrylates include 1,4-butanediol dimethacrylate, tetraethylene glycol dimethacrylate and Bisphenol A dimethacrylate. Examples of suitable trimethacrylates include trimethylolpropane trimethacrylate The sizing compound used in the method according to the invention can also be a multifunctional acrylate polymer. Multifunctional acrylate polymers are selected from the group consisting of epoxy acrylate polymers, urethane acrylate polymers, polyester acrylate polymers and mixtures thereof. Suitable epoxy acrylate polymers include Bisphenol A epoxy diacrylate, available from Sartomer Company, Inc. of Exton, Pa. Bisphenol A epoxy diacrylate is sold under the designation CN104. CN104 has a viscosity of 3,500 mPa·s at 65°C. and a specific gravity of 1.15. Suitable urethane acrylate polymers include hexafunctional aromatic urethane acrylate with an acrylated polyol diluent, which is available under the designation Ebecryl-220™. Ebecryl-220™ has a number average molecular weight of 1,000 and a viscosity of 28,000 mPa·s at 25°C. Another suitable urethane acrylate is aliphatic urethane diacrylate, which is available under the designation Ebecryl-230™. Ebecryl-230™ has a number average molecular weight of 5,000 and a viscosity of 40,000 mPa·s at 25°C. Both of these urethane acrylates are available from UCB Radcure, Inc. of Louisville, Ky. Suitable polyester acrylate polymers include tetrafunctional polyester acrylate, which is available under the designation Ebecryl-80™ by UCB Radcure, Inc. Ebecryl-80™ has a number average molecular weight of 1,000 and a viscosity of 3,500 mPa·s at 25°C. Urethane acrylate polymers are preferred for the sizing compound of this invention. Ebecryl-220™ is particularly preferred. The curing agent used for the non-aqueous sizing composition is selected from the group consisting of ultra-violet photoinitiators and free radical initiators. Preferably, the curing agent is an ultra-violet photoinitiator. When the curing agent is an ultra-violet photoinitiator, the amount present is 1to 20%, preferably 2 to 8%, by weight of the non-aqueous sizing composition. The ultra-violet photoinitiator can be any compound that will start a reaction with the sizing compound when exposed to ultra-violet radiation. The ultra-violet photoinitiator must be compatible with the other ingredients of the composition used in the present invention. Compatibility can be determined by mixing 1 weight percent of the ultra-violet photoinitiator with the other ingredients of the composition at room temperature. The photoinitiator is compatible if no precipitate forms. Another requirement for the photoinitiator is that it not cause the composition to react in the absence of ultra-violet radiation. Suitable compounds for this ultra-violet photoinitiator include benzophenone, acetonaphthone, acetophenone, benzoin methyl ether, benzoin isobutyl ether, 2-hydroxy-2-methyl-1-phenylpropan-1-one, 1-hydroxycyclohexylphenyl ketone, diethoxyacetophenone, hydroxypropylphenyl ketone and hydroxypropylisopropylphenyl ketone. 2-Hydroxy-2-methyl-1-phenylpropan-1-one is preferred. In an alternative embodiment, the curing agent may be a free radical initiator. When the curing agent is a free radical initiator, the amount present in the. sizing composition is 1 to 20%, preferably 4 to 8%, by weight of the total composition. Suitable free radical initiators include peroxide compounds such as benzoyl peroxide or 2,4-dichlorobenzoyl peroxide and vazo compounds such as azobisisobutyronitriles. The non-aqueous sizing composition may also contain an optional dry solvent. "Dry" means that the solvent contains less than 200 ppm by weight of water, preferably less than 100 ppm by weight of water. Suitable solvents for the present invention include alcohols such as methyl, ethyl, isopropyl and t-butyl; aromatic hydrocarbons such as benzene, toluene and xylene; aliphatic hydrocarbons such as heptane, hexane and octane; glycol ethers such as propylene glycol methyl ether, dipropylene glycol, methyl ether, propylene glycol n-butyl ether, propylene glycol n-propyl ether and ethylene glycol n-butyl ether; and halogenated hydrocarbons such as 1,1,1-trichloroethane and methylene chloride. Toluene and isopropyl alcohol are preferred. The amount of solvent in the curable sizing composition is up to 98%, preferably 1 to 98%, and more preferably 60 to 80% by weight. The present invention thus provides a method of producing a sized fiber, wherein said method comprises applying an interfacial coating to the ceramic fiber and subsequently applying the non-aqueous sizing composition to a fiber and thereafter curing the sizing compound to form a sized fiber. If the sizing composition contains a solvent, the solvent may be removed after applying the non-aqueous sizing composition to the fiber and before curing the sizing compound. The fibers of the present invention are selected from silicon carbide fibers, silicon oxycarbide fibers, silicon oxynitride fibers, silicon carbide fibers containing titanium, silicon oxycarbonitride fibers, silicon nitride fibers. Preferably, the ceramic fibers are silicon oxycarbonitride fibers. Ceramic fibers are useful in composites, such as resin matrix, metal matrix and ceramic matrix composites; and such fibers are well known in the art. Methods for preparing ceramic fibers derived from hydridopolysiliazanes are also known in the art. For example, U.S. Patent 5,547,623 enumerates a method of preparing ceramic fibers from a hydridopolysilazane resin by melt spinning the resin into a fiber, then curing the outer surface of the fiber and thereafter continuously pyrolyzing the fiber. Methods for preparing this ceramic fiber are not specifically restricted. Commercially available fibers may be supplied with a surface sizing. Preferably, the sizing is removed herein and subsequently an interfacial coating is applied over fibers. This interfacial coating improves strength and toughness of a composite and/or a matrix made from these fibers. The interfacial coating on the ceramic fibers produced by the method according to the invention is exemplified by carbon, boron nitride, silicon carbide, silicon nitride and mixtures thereof. The fibers are preferably coated with boron nitride for most commercial applications. Some interfacial coatings react with water; therefore, the sizing composition must be non-aqueous. Methods for coating the fibers with interfacial coatings are known in the art and are not critical. For example, fibers can be coated by vapor deposition of borazine at temperatures less than 1000°C., see for example, U.S. Patent 4,642,271. The amount of coating depends on the type and diameter of the fibers; however, the amount of coating on our fibers is preferably 0.1 to 0.7 micrometers in thickness. The coated ceramic fibers produced by the method of the present invention typically have diameter of 9 to 20 micrometers, preferably 15 to 20 micrometers. The coated ceramic fibers of this invention also typically have a fineness of 900 to 1800 g per 9000 m. The sizing composition may then be applied to our coated ceramic fibers by dipping, spraying, roll coating, extruding, pultrusion or vapor deposition. Preferably, the composition is applied to the coated fibers continuously. When the curable sizing composition is applied continuously, the composition is typically applied at a race of 0.5 to 2.0, preferably 0.8 to 1.5 grams per minute. If solvent is present in the claimed non-aqueous sizing composition, the solvent is removed after said composition is applied to the fiber and before its cure. The solvent may be removed by heating the fiber to evaporate the solvent, allowing the solvent to evaporate at ambient temperature and pressure or by subjecting the fiber to vacuum. When the solvent is removed by heating, the required temperature will vary depending on the solvent and type of fiber used. Ceramic fibers are preferably heated to a temperature up to 100°C. when the solvent is toluene. However, the temperature to which the fiber is heated must be less than the boiling point of the solvent. The solvent is preferably removed continuously, for example, by passing the fiber through a heater, such as a tube furnace. The time required to remove the solvent will vary depending on the temperature and the solvent; however, the time required is typically several seconds to several hours and preferably 10 to 20 seconds. The sizing compound is then cured to form a sized, coated fiber. When the curing agent is an ultra-violet photoinitiator, the sizing compound cures by exposure to ultra-violet radiation. Sources of ultra-violet radiation are well known in the art and are not critical. For example, the ultra-violet radiation source may be a mercury lamp such as a Colight Model UV-6™. The intensity of the ultra-violet radiation required to cure the sizing compound is 100 to 4,000, preferably 300 to 2,000, mJ/cm 2 . The time required to cure the sizing compound is speed dependent. Usually, the time required to cure the sizing compound is 0.01 to 10, preferably 0.5 to 5 seconds at a rate of 0.3 m/s. When the curing agent is a free radical initiator, the sizing compound cures by heating. The temperature required to cure the sizing compound depends upon the free radical initiator and the type of fiber used. Normally, the temperature required is up to 400°C. When the free radical initiator is benzoyl peroxide, the temperature ranges up to 120°C., preferably 100 to 120°C. When the free radical initiator is an azobisisobutyronitrile, the temperature used is 120 to 400°C., preferably 150 to 250°C. The time required to cure the sizing compound is speed dependent and ranges between 0.1 to 30 seconds, preferably 1 to 20 seconds at a rate of 0.3 m/s. The resulting sized, coated fibers of this invention are preferably collected continuously. For example, the fibers may be wound onto a spool using a Kamitsu™ fiber winder. For most applications, the fiber is collected at a rate up to 0.3 m/s. The sized fibers may then be woven into any desired shape; for example, two-dimensional fabrics and three-dimensional pre-forms. After weaving, the sizing can be removed by heating at a relatively low temperature (less than 500°C.) under an inert atmosphere. The inert atmosphere preferably comprises argon or nitrogen, where inert is defined as containing less than 500 ppm oxygen. Heating under an inert atmosphere leaves little or no residue on our fibers. Char yield is the weight percent of residue remaining on the fiber after heating. Typically, char yield is 5% by weight, or even less. Preferably, char yield is less than 1% by weight with no carbon or other reactive species, such as sulfides, metals and nitrides. These examples are intended to illustrate and clarify our invention to those skilled in the art. In the following examples, BN means boron nitride and SiC means silicon carbide. Comparative Example Two mixtures were evaluated for use as non-aqueous sizing compositions. The ingredients of Comparative Mixtures 1 and 2 are summarized in Table 1. Thermogravimetric analysis was performed on each mixture by heating the mixture in flowing nitrogen to 1200°C. Weight loss and char yield for each mixture were determined and are reported in Table 2. Char yield was greater than 5% for both mixtures. Example Two additional mixtures were evaluated for use as non-aqueous sizing compositions. The ingredients of the Mixtures 1 and 2 are summarized in Table 1. Thermogravimetric analysis was conducted on each of the mixtures by heating the mixture in flowing nitrogen to 1200°C. Weight loss and char yield for each mixture are reported in Table 2. Both mixtures had char yields of less than 5%. Components Comparative Mixture 1 Comparative Mixture 2 Mixture 1 Mixture 2 50% acrylate silica silane 5 g - - - tetraethyl orthosilicate - 5 g - - trimethylolpropane triacrylate - - 5 g - urethane acrylate - - - 5 g photoinitiator 0.2 g 0.2 g 0.2 g 0.2 g isopropanol 25 g - 25 g - toluene - 25 g - 25 g Mixture % Weight Loss, Maximum Temperature at which Max Weight Loss Occurred °C Char Yield % Comparative 1 65 % 442 °C 35% Comparative 2 84 % 468 °C 15% 1 97 % 450 °C 3% 2 100 % 390 °C ≤1% Example 2 Mixture 2 from Table 1 was then applied to a boron nitride coated, silicon oxycarbonitride fiber tow (1000 g per 9000 m) according to the following continuous method: The coated fiber, wound on a spool, was threaded through a sizing applicator. A 17 % concentration of Mixture 2 was then pumped to the sizing applicator by a peristaltic pump at a rate sufficient to apply 0.8g per minute of sizing to the fiber. The fiber next passed through a tube furnace at 100°C. to remove the toluene. The fiber was subsequently passed through an ultra-violet unit (Colight™ Model UV-6, 300 Watts) to cure the coating. The fiber was thereafter wound on a cardboard spool using a Kamitsu™ fiber winder at a speed of 0.3 m per second. The sized coated fiber was successfully woven into a three-dimensional pre-form that was further processed into a ceramic matrix composite by conventional methods. This process was then repeated to size the boron nitride coated, silicon carbide fiber tow (1800 denier) [1980 x 10 -7 kg/m) instead of the boron nitride coated, silicon oxycarbonitride fiber tow. The sized coated silicon carbide fiber tow was successfully used for filament winding of composite tubes.

Claims: A method of producing a sized ceramic fiber comprising the steps of: (1) applying to the ceramic fiber an interfacial coating; and subsequently (2) applying to the ceramic fiber selected from silicon carbide fibers, silicon oxycarbide fibers, silicon oxynitride fibers, silicon carbide fibers containing titanium, silicon oxycarbonitride fibers, and silicon nitride fibers a non-aqueous sizing composition essentially consisting of: (a) 1 to 98% by weight of a sizing compound selected from multifunctional acrylate monomers, multifunctional methacrylate monomers and multifunctional acrylate polymers, and (b) 1 to 20% by weight of a curing agent selected from ultra-violet photoinitiators and free-radical initiators; and thereafter (3) curing the sizing compound to form a sized ceramic fiber. The method according to claim 1 wherein said interfacial coating is selected from carbon, boron nitride, silicon carbide, silicon nitride and mixtures thereof. The method according to claim 1 or 2, wherein ingredient (a) is a multifunctional acrylate monomer selected from diacrylates, triacrylates, tetracrylates and pentaacrylates. The method according to claim 3 wherein the multifunctional acrylate monomer is trimethylol propane triacrylate. The method according to claim 1 or 2, wherein ingredient (a) is a multifunctional acrylate polymer selected from epoxy acrylate polymers, urethane acrylate polymers, polyester acrylate polymers and mixtures thereof. The method according to claim 5, wherein the multifunctional acrylate polymer is hexafunctional aromatic urethane acrylate with an acrylated polyol diluent. The method according to any of claims 1 to 6, wherein ingredient (b) is an ultra-violet photoinitiator selected from benzophenone, acetonaphthone, acetophenone, benzoin methyl ether, benzoin isobutyl ether, 2-hydroxy-2-methyl-1-phenylpropan-1-one, 1-hydroxycyclohexylphenyl ketone, diethoxyacetophenone, hydroxypropylphenyl ketone and hydroxypropylisopropylphenyl ketone. The method according to claim 7, wherein the ultra-violet photoinitiator is 2-hydroxy-2-methyl-1-phenylpropan-1-one present at 2 to 8% by weight of the sizing composition. The method according to any of claims 1 to 8, wherein the sizing composition further comprises 1 to 98% by weight of the composition of a dry solvent. The method according to claim 9, wherein said solvent is removed after the composition is applied to the ceramic fiber and before the sizing compound is cured. The method according to claim 10, wherein the solvent is toluene and it is removed by heating to a temperature up to 100°C. The method according to any of claims 1 to 11, wherein the non-aqueous sizing composition is applied to the ceramic fiber by a method selected from dipping, spraying, roll coating, extruding, pultrusion and vapor deposition. The method according to any of claims 1 to 12, wherein the sizing compound cures by exposure to ultra-violet radiation with an intensity of 100 to 4000 mJ/cm 2 . The method according to any of claims 1 to 13, further comprising the heating of the sized ceramic fiber to a temperature up to 500°C. under an inert atmosphere to remove the sizing compound. The method of according to claim 14, wherein the char yield after said heating is up to 5% by weight based on the weight of sizing compound applied to the fiber. The method according to claim 15 wherein the char yield is ≤1% by weight.

Inventors: BLIZZARD JOHN DONALD, SZWEDA ANDREW, WIEBER GARY MICHAEL, BLIZZARD, JOHN DONALD, SZWEDA, ANDREW, WIEBER, GARY MICHAEL
Applicants: COI CERAMICS INC, COI CERAMICS, INC.
Application year: 1999
Main classification: C04B35
IPC codes: D06M101, C08F299, C04B35, C03C25, D06M15