US3676179A - Coated article and method for making same - Google Patents

Coated article and method for making same Download PDF

Info

Publication number
US3676179A
US3676179A US764954A US3676179DA US3676179A US 3676179 A US3676179 A US 3676179A US 764954 A US764954 A US 764954A US 3676179D A US3676179D A US 3676179DA US 3676179 A US3676179 A US 3676179A
Authority
US
United States
Prior art keywords
carbon
article
coating
coated
thermal expansion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US764954A
Inventor
Jack C Bokros
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
General Atomics Corp
Gulf Oil Corp
Original Assignee
Gulf Oil Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Gulf Oil Corp filed Critical Gulf Oil Corp
Application granted granted Critical
Publication of US3676179A publication Critical patent/US3676179A/en
Assigned to GA TECHNOLOGIES INC., A CA CORP. reassignment GA TECHNOLOGIES INC., A CA CORP. ASSIGNS ENTIRE INTEREST. SUBJECT TO REORGANIZATION AGREEMENT DATED JUNE 14, 1982 Assignors: GENERAL ATOMIC COMPANY
Assigned to GENERAL ATOMICS reassignment GENERAL ATOMICS CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). EFFECTIVE DATE: FEBRUARY 1, 1988. Assignors: GA TECHNOLOGIES, INC.,
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B41/00After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
    • C04B41/45Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
    • C04B41/50Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials
    • C04B41/5001Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements with inorganic materials with carbon or carbonisable materials
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/22Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/22Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
    • C23C16/26Deposition of carbon only
    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21CNUCLEAR REACTORS
    • G21C3/00Reactor fuel elements and their assemblies; Selection of substances for use as reactor fuel elements
    • G21C3/42Selection of substances for use as reactor fuel
    • G21C3/58Solid reactor fuel Pellets made of fissile material
    • G21C3/62Ceramic fuel
    • G21C3/626Coated fuel particles
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/26Web or sheet containing structurally defined element or component, the element or component having a specified physical dimension
    • Y10T428/263Coating layer not in excess of 5 mils thick or equivalent
    • Y10T428/264Up to 3 mils
    • Y10T428/2651 mil or less
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/30Self-sustaining carbon mass or layer with impregnant or other layer

Definitions

  • Deposition of pyrolytic carbon is effected on an article from a carbonaceous atmosphere at a preselected temperature under conditions that result in formation of canbon having a preselected coefiicient of thermal ex pansion which is less than that of the article.
  • the difference between the coeflicients of thermal expansion of the article and the pyrolytic carbon causes the pyrolytic carbon coating to be placed under substantial compressive tangential stress.
  • Deposition is usually carried out at a temperature of about 1500 C. or below to deposit fairly dense isotropic or laminar carbon.
  • the coefficient of thermal expansion of the article being coated is usually between about 6 to 9 10- C., with the preferred material being graphite.
  • the present invention relates generally to the coating of articles and, more particularly, it relates to methods of coating articles with pyrolytic carbon and to the products of such methods.
  • Coating articles with pyrolytic canbon is a known coating operation. Generally, it is carried out by deposition onto the articles of pyrolytic carbon formed by high temperature decomposition (pyrolysis) of carbonaceous substances, such as volatile or gaseous hydrocarbons.
  • pyrolysis high temperature decomposition
  • carbonaceous substances such as volatile or gaseous hydrocarbons.
  • US. Letters Patent No. 3,298,921 there are disclosed various specific examples of effecting such deposition and the types of crystalline pyrolytic carbon formed are defined. The disclosure of this patent is incorporated herein by reference.
  • a preferred method of coating dis closed in that patent involves a fluidized bed process in which the hydrocarbon gas, or a mixture of the hydrocarbon gas with a carrier gas, is utilized to levitate a bed of the articles being coated.
  • elevated temperatures are used to produce decomposition of the hydrocarbon gas.
  • decomposition temperatures vary between, for example, 800 C. and 2300 C. At such elevated temperatures the hydrocarbon gas decomposes and elemental carbon is deposited on the articles.
  • various diflFerent types of pyrolytic carbon are obtained.
  • at least three different carbon structures may be obtained, namely, laminar carbon, isotropic carbon and granular carbon.
  • the strengths of these types of pyrolytic carbon vary, and when it is desired to obtain high strength characteristics in the pyrolytic carbon deposited, the stronger carbon types, i.e., isotropic and laminar carbon, are used.
  • a further object is to provide strong pyrolytic carbon-coated articles.
  • pyrolytic carbon has greater structural strength under compressive stress than under tensile stress. It is possible to take advantage of its higher compressive strength to provide a coated article having high structural strength. The use of these relatively high temperatures necessary to obtain pyrolysis of the hydrocarbon gas and consequent deposition on the article being coated facilitates the obtaining of this objective because of the significant temperature differential available.
  • the materials of which the articles to be coated may be made are somewhat limited. Such material, sometimes referred to herein as the substrate, should not lose substantial strength at pyrolysis temperatures and should not chemically react with the substances in the pyrolysis zone.
  • suitable substrate materials include carbon (graphite in particular), tantalum, tungsten, molybdenum, alloys thereof, and refractory materials in general, such as mullite.
  • the coefficient of thermal expansion of potential substrate materials is usually known, or if not known can readily be determined. For purposes of the present applications, substrates are usually chosen having coeflicients of thermal expansion between about 6 to 9X l0 C.
  • the article to be coated is disposed in the zone wherein pyrolysis is to be carried out and is heated therein to a preselected temperature.
  • This temperature is functionally related to the type of carbon to be deposited, to the desired coefiicient of thermal expansion of the deposited carbon, and to the magnitude of the final compressive tangential stress that is attained in the cool coated article.
  • the temperature and the other coating conditions are accordingly chosen to provide the particular crystalline type of carbon desired and to provide a preselected coefiicient of thermal expansion of the carbon which is less than the coelficient of thermal expansion of the substrate material.
  • the pyrolytic carbon employed should complement this objective.
  • the density of the pyrolytic carbon deposited should be at least about 1.5 gm./cm. because porous carbons do not exhibit as high resistance to compression as do more dense carbons.
  • hte pyrolytic carbon coating should be thick enough to provide such strength. Accordingly, the pyrolytic carbon coating will be at least about 25 microns thick and usually will have a thickness of microns or more.
  • isotropic carbon is preferred because it exhibits no tendency to delaminate and because stresses due to anisotropic expansion do not arise in isotropic coatings on irregular shapes at locations where small radii of curvature are encountered.
  • Isotropic carbon having an apparent crystallite size of about 50 A. or less and which is deposited at between about 1200 C. and 1500 C. is generally preferred.
  • Cooling of the coated article from the elevated deposition temperature results in shrinkage or contraction of both the substrate material and the coating.
  • the bond between the carbon coating and the substrate must be sufficiently strong and the coefiicient of thermal expansion of the pyrolytic carbon coating should not be so much different than the coefficient of thermal expansion of the substrate as to break or rupture the bond.
  • the coefficient of thermal expansion of the carbon should certainly not be greater than the coefficient of thermal expansion of the substrate material least the coating be placed in tension upon cooling, rendering it more susceptible to fracture.
  • the coefficient of thermal expansion of the pyrolytic carbon coating is selectively less than that of the substrate material so that, upon cooling of the coated article, the substrate material contracts more than the coating and places the coating under compressive tangential stress.
  • the difference in coefficients should not be so great that, upon cooling, the compressive fracture stress of the coating is reached (which would result in failure of the coating) or the substrate separates from the coating at the interface therebetween.
  • the magnitude of the compressive tangential stress in the coating material after cooling is dependent not only on the difference in coeificients of thermal expansion of the respective material, but also upon the temperature differential between deposition temperature and ambient temperature.
  • the prospective temperature difference is therefore taken into consideration in determining the desired coefiicient of thermal expansion for the pyrolytic carbon to be deposited. Because of the different interrelated variable to be considered, no set numerical value can be definitively stated; however, usually the thermal coefficient of expansion of the substrate will not be more than about 50 percent greater than that of the carbon coating.
  • the coated article will be used at temperatures other than ambient temperature, then the temperature of intended use is also taken into consideration.
  • the coating should be under tangential compressive stress both at ambient temperature and at the temperature of use, if they are different.
  • the modulus of rupture of pyrolytic carbon deposited at about 1500 C. or below should exceed 30,000 p.s.i. tangential compressive stress has been obtained in pyrolytic carbon coatings between about 5000 and 30,000 p.s.i. with the resultant coated articles exhibiting high structural strengths. Tangential compressive stress at least as high as 20,000 p.s.i., may be obtained using a substrate made of graphite to which the pyrolytic carbn forms an excellent bond. An actual upper limit of the tangential compressive strength has not been determined and will presumably be dependent at least in part upon the substrate material and how strong a bond is obtained thereto. In general when this upper limit is exceeded, if the carbon layer is relatively thick, debonding occurs, and if the carbon coating is thin, compressive failure of the carbon layer occurs.
  • Articles of various geometric configurations may be coated in accordance with the present invention.
  • the coated articles will have a largest dimension at least equal to one-half inch inasmuch as the strength of the article is a desired advantage.
  • smaller articles might be desirable.
  • Spheres, rods and even tubes are examples of such articles that may be fabricated having good structural strength.
  • Both examples employ the generally preferred methods of depositing isotropic carbon at temperatures below about 1500 C.
  • it is generally not substantially more difiicult to deposit isotropic carbon at temperatures below about 1500 C. than to deposit laminar carbon or higher temperature isotropic carbon. Accordingly, because such lower temperature isotropic carbons can be deposited having a BAF of 1.1 or less, apparent crystallite sizes of 50 A. or less and a density up to about 2.0 g./cm. they are usually employed because they have greater strength and greater wearability.
  • isotropic carbon deposited at temperatures above about 1500 C., as from methane or propane or the like might be used for many applications.
  • Laminar carbon which as deposited from methane at temperatures below 1500 C. has a apparent crystallite size of about 50 A. or less and has a density greater or equal to about 1.5 g./cc., may adequately fill the requirements of many applications.
  • a generally spherical article is chosen made of graphite having a coelficient of thermal expansion of about 8Xl0- C.
  • the spheroid approximately inch in diameter, is lightly sandblasted to remove any loose particles and is placed in a vertical graphite reaction tube.
  • the tube is about 6.3 centimeters in diameter and is heated to a temperature of about vl400 C. while a how of helium gas therethrough is maintainend.
  • the spheroid plus an ancillary charge of grams of zirconium dioxide particles to provide additional available deposition surface area as explained in UJS. Pat. 3,399,969) having an average particle size of about 400 microns are loaded into the reaction tube.
  • Propane gas is admixed with the helium to provide a partial pressure of propane of about 0.3 atm. (total pressure of 1 atm.). The total flow of gas is held at about 4000 cc. per minute.
  • the propane undergoes pyrolysis and deposits carbon, Carbon is deposited on the spheroid in the form of isotropic pyrolytic carbon having a coefficient of thermal expansion of about 5X l0- C. Subsequent examination also shows the carbon has a BAF of about 1.1, an apparent crystallite size of about 40 A. and a density of about 1.7 grams per cm. Deposition is continued until an isotropic pyrolytic carbon coating about 6 mils microns) thick is obtained, a time of about an hour.
  • the resultant coated sphere is allowed to cool to ambient temperature and is removed from the reaction tube.
  • the change in temperature of nearly 1400 C. between the deposition temperature and ambient temperature effects a sufiiciently greater contraction of the substrate carbon spheroid than of the isotropic car-bon coating to set up a circumferential compressive stress in the coating of about 15,000 p.s.i. This stress is well below the estimated compressive fracture stress of the coating.
  • the resultant coated article is considered to have high structural strength.
  • a control article which is similarly coated with pyrolytic isotropic carbon which has a greater coefficient of thermal expansion than the carbon substrate, so that its circumference is under tensile strength, will fracture upon being dropped from a height of about three feet.
  • the coated article described above having its outer coating in compressive stress may be dropped repeatedly from the same height Without damage.
  • Other tests show the coated spheroid exhibits not only good resistance to fracture, but also good wearresistance.
  • EXAMPIJE II A graphite spheroid similar to that coated in Example I is introduced into the same reaction tube which is heated to a temperature of about 1350 C. while maintaining 21 flow of helium gas through it.
  • a similar ancillary charge of 100 grams of Zr particles is loaded into the reaction tube.
  • Propane gas is admixed with the helium to provide a gas flow of about 8000 cc. per minute having a partial pressure of propane of about 0.4 atm. (total pressure of 1 atm.). All of the helium is bubbled through methyltrichlorosilane.
  • the propane and the methyltrichlorosilane pyrolyze to deposit a mixture of isotropic carbon and silicon carbide on the spheroid. Deposition is continued until a coating about 8 mils (200 microns) thick is obtained, a time of about an hour.
  • the resultant coated sphere is allowed to cool to ambient temperature and is removed from the reaction tube.
  • Examination of the isotropic carbon-silicon carbide coating shows it has a coefiicient of thermal expansion of about 6 10 C. and a density of about 2 grams per cmfi.
  • the coating contains about .10 weight percent silicon, in the form of silicon carbide.
  • the isotropic carbon has a BAF of about 1.1 and an apparent crystallite size of about 35 A.
  • the change in temperature effects a sufliciently greater contraction of the substrate spheroid than of the coating to set up a circumferential compressive stress in the coating of about 10,000 p.s.i. This stress is well below the estimated compressive fracture stress of the coating.
  • the resultant coated article is considered to have excellent structural strength.
  • the coated spheroid may be dropped repeatedly from about three feet without damage. Other tests show the coated spheroid exhibits not only good resistance to fracture, but also good wearresistance.
  • the isotropic carbon-silicon carbide coating is considered to have all the advantages from the standpoint of strength and wearability as the completely carbon coating produced in Example I. Moreover, with other coating variables being maintained generally equal, it is considered that an isotropic carbon coating that is deposited with a silicon carbide additive will have greater strength than the same isotropic carbon without the additive. In general, it is considered that up to about 15 percent by weight of silicon, or an equivalent amount of a similar carbide-forming additive, may be included without detracting from the desirable properties of the pyrolytic carbon coatings as described hereinbefore.
  • a coated article having high strength characteristics which comprises an article made of graphite having a coefficient of thermal expansion between 6 to 9 X 10- C. and a coating of pyrolytic carbon surrounding said graphite article which pyrolytic carbon was deposited thereupon at a temperature well above ambient and which has a strong bond to said underlying graphite article, said pyrolytic carbon having a density of at least 1.5 -g./ cc. and having a coefficient of thermal expansion which is less than that of the graphite article and being under substantial compressive tangential stress as a result of the thermal contraction occurring during cooling the coated graphite article from deposition temperature to ambient temperature.
  • a method of forming an article having high strength characteristics comprises heating a graphite article having a coefficient of thermal expansion between 6 and 9X 10-/ C. to a preselected deposition temperature of at least about 1200 C., effecting deposition of pyrolytic carbon on said graphite article from a carbonaceous atmosphere at said preselected temperature under conditions that result in formulation of carbon having a density of at least 1.5 g./cc.
  • a method in accordance with claim 9 wherein the thickness of said pyrolytic carbon coating is at least about 25 microns.
  • said pyrolytic carbon coating is isotropic carbon having an apparent crystallite size of about 50 A. or less.

Abstract

A METHOD OF COATING WITH PYROLYTIC CARBON TO PROVIDE A COATED ARTICLE HAVING HIGH STRENGTH CHARACTERISTICS. DEPOSITION OF PYROLYTIC CARBON IS EFFECTED ON AN ARTICLE FROM A CARBONACEOUS ATMOSPHERE AT A PRESELECTED TEMPERATURE UNDER CONDITIONS THAT RESULT IN FORMATION OF CARBON HAVING A PRESELECTED COEFFICIENT OF THERMAL EXPANSION WHICH IS LESS THAN THAT OF THE ARTICLE. DURING COOLING OF THE COATED ARTICLE TO AMBIENT TEMPERATURE, THE DIFFERENCE BETWEEN THE COEFFICIENTS OF THERMAL EXPANSION OF THE ARTICLE AND THE PYROLYTIC CARBON CAUSES THE PYTOLYTIC CARBON COATING TO BE PLACED UNDER, SUBSTANTIAL COMPRESSIVE TANGENTIAL STRESS. DEPOSITION IS USUALLY CARRIED OUT AT A TEMPERATURE OF ABOUT 1500*C. OR BELOW TO DEPOSIT FAIRLY DENSE ISOTROPIC OR LAMINAR CARBON. THE COEFFICIENT OF THERMAL EXPANSION OF THE ARTICLE BEING COATED IS USUALLY BETWEEN ABOUT 6 TO 9X10**-4/0C., WITH THE PREFERRED MATERIAL BEING GRAPHITE.

Description

United States Patent 3,676,179 COATED ARTICLE AND METHOD FOR MAKING SAME Jack C. Bokros, San Diego, Calif., assignor to Gulf Oil Corporation, San Diego, Calif. No Drawing. Filed Oct. 3, 1968, Ser. No. 764,954 Int. Cl. C23c 11/10; B44d 1/12 U.S. Cl. 11746 'CG 15 Claims ABSTRACT OF THE DISCLOSURE A method of coating with pyrolytic carbon to provide a coated article having high strength characteristics. Deposition of pyrolytic carbon is effected on an article from a carbonaceous atmosphere at a preselected temperature under conditions that result in formation of canbon having a preselected coefiicient of thermal ex pansion which is less than that of the article. During cooling of the coated article to ambient temperature, the difference between the coeflicients of thermal expansion of the article and the pyrolytic carbon causes the pyrolytic carbon coating to be placed under substantial compressive tangential stress. Deposition is usually carried out at a temperature of about 1500 C. or below to deposit fairly dense isotropic or laminar carbon. The coefficient of thermal expansion of the article being coated is usually between about 6 to 9 10- C., with the preferred material being graphite.
The present invention relates generally to the coating of articles and, more particularly, it relates to methods of coating articles with pyrolytic carbon and to the products of such methods.
Coating articles with pyrolytic canbon is a known coating operation. Generally, it is carried out by deposition onto the articles of pyrolytic carbon formed by high temperature decomposition (pyrolysis) of carbonaceous substances, such as volatile or gaseous hydrocarbons. In US. Letters Patent No. 3,298,921, there are disclosed various specific examples of effecting such deposition and the types of crystalline pyrolytic carbon formed are defined. The disclosure of this patent is incorporated herein by reference. A preferred method of coating dis closed in that patent involves a fluidized bed process in which the hydrocarbon gas, or a mixture of the hydrocarbon gas with a carrier gas, is utilized to levitate a bed of the articles being coated.
In fluidized bed coating, and in other known alternative methods for depositing pyrolytic carbon, elevated temperatures are used to produce decomposition of the hydrocarbon gas. Such decomposition temperatures vary between, for example, 800 C. and 2300 C. At such elevated temperatures the hydrocarbon gas decomposes and elemental carbon is deposited on the articles.
By suitable selection of temperature, carbonaceous substance and other operating variables, various diflFerent types of pyrolytic carbon are obtained. As set forth in the foregoing patent, at least three different carbon structures may be obtained, namely, laminar carbon, isotropic carbon and granular carbon. The strengths of these types of pyrolytic carbon vary, and when it is desired to obtain high strength characteristics in the pyrolytic carbon deposited, the stronger carbon types, i.e., isotropic and laminar carbon, are used.
It is an object of the present invention to provide a method of depositing pyrolytic carbon wherein high structural strength is obtained. A further object is to provide strong pyrolytic carbon-coated articles.
Generally, in accordance with the present invention,
3,676,179 Patented July 11, 1972 ice the conditions of pyrolytic carbon deposition are carefully controlled to deposit pyrolytic carbon having a coefficient of thermal expansion less than the coefficient of thermal expansion of the article to be coated so that, after the coated article cools to room temperature, the pyrolytic carbon is under compressive tangential stress. It is believed that any substantial compressive tangential stress that is created increases the structural strength of the coated article and that the greater the magnitude of the tangential compressive stress, the greater is the resultant strength of the coated article, until an upper limit is reached as discussed hereinafter. The carbons of primary interest are isotropic carbons deposited at temperatures of about 1500 C. or below, which carbons have a modulus of rupture in the range of 30,000 to 70,000 p.s.i. and are thus well capable of withstanding these tangential compressive stresses.
More particularly, pyrolytic carbon has greater structural strength under compressive stress than under tensile stress. It is possible to take advantage of its higher compressive strength to provide a coated article having high structural strength. The use of these relatively high temperatures necessary to obtain pyrolysis of the hydrocarbon gas and consequent deposition on the article being coated facilitates the obtaining of this objective because of the significant temperature differential available.
Because of the high temperatures at which pyrolysis is carried out, the materials of which the articles to be coated may be made are somewhat limited. Such material, sometimes referred to herein as the substrate, should not lose substantial strength at pyrolysis temperatures and should not chemically react with the substances in the pyrolysis zone. Examples of suitable substrate materials include carbon (graphite in particular), tantalum, tungsten, molybdenum, alloys thereof, and refractory materials in general, such as mullite. The coefficient of thermal expansion of potential substrate materials is usually known, or if not known can readily be determined. For purposes of the present applications, substrates are usually chosen having coeflicients of thermal expansion between about 6 to 9X l0 C.
The article to be coated is disposed in the zone wherein pyrolysis is to be carried out and is heated therein to a preselected temperature. This temperature, as subsequently set forth, is functionally related to the type of carbon to be deposited, to the desired coefiicient of thermal expansion of the deposited carbon, and to the magnitude of the final compressive tangential stress that is attained in the cool coated article. The temperature and the other coating conditions are accordingly chosen to provide the particular crystalline type of carbon desired and to provide a preselected coefiicient of thermal expansion of the carbon which is less than the coelficient of thermal expansion of the substrate material.
Because one of the objectives of the coating operation is to provide a product having high structural strength, the pyrolytic carbon employed should complement this objective. Generally, the density of the pyrolytic carbon deposited should be at least about 1.5 gm./cm. because porous carbons do not exhibit as high resistance to compression as do more dense carbons. Likewise, because good structural strength is a criterion of the resultant product, hte pyrolytic carbon coating should be thick enough to provide such strength. Accordingly, the pyrolytic carbon coating will be at least about 25 microns thick and usually will have a thickness of microns or more. Although both laminar and isotropic carbons can be employed to produce coated articles having good structural strength, isotropic carbon is preferred because it exhibits no tendency to delaminate and because stresses due to anisotropic expansion do not arise in isotropic coatings on irregular shapes at locations where small radii of curvature are encountered. Isotropic carbon having an apparent crystallite size of about 50 A. or less and which is deposited at between about 1200 C. and 1500 C. is generally preferred.
Cooling of the coated article from the elevated deposition temperature results in shrinkage or contraction of both the substrate material and the coating. To obtain the desired compressive tangential stress, the bond between the carbon coating and the substrate must be sufficiently strong and the coefiicient of thermal expansion of the pyrolytic carbon coating should not be so much different than the coefficient of thermal expansion of the substrate as to break or rupture the bond. On the other hand however, the coefficient of thermal expansion of the carbon should certainly not be greater than the coefficient of thermal expansion of the substrate material least the coating be placed in tension upon cooling, rendering it more susceptible to fracture. The coefficient of thermal expansion of the pyrolytic carbon coating is selectively less than that of the substrate material so that, upon cooling of the coated article, the substrate material contracts more than the coating and places the coating under compressive tangential stress. However, the difference in coefficients should not be so great that, upon cooling, the compressive fracture stress of the coating is reached (which would result in failure of the coating) or the substrate separates from the coating at the interface therebetween.
The magnitude of the compressive tangential stress in the coating material after cooling is dependent not only on the difference in coeificients of thermal expansion of the respective material, but also upon the temperature differential between deposition temperature and ambient temperature. The prospective temperature difference is therefore taken into consideration in determining the desired coefiicient of thermal expansion for the pyrolytic carbon to be deposited. Because of the different interrelated variable to be considered, no set numerical value can be definitively stated; however, usually the thermal coefficient of expansion of the substrate will not be more than about 50 percent greater than that of the carbon coating.
If the coated article will be used at temperatures other than ambient temperature, then the temperature of intended use is also taken into consideration. Preferably, the coating should be under tangential compressive stress both at ambient temperature and at the temperature of use, if they are different.
The modulus of rupture of pyrolytic carbon deposited at about 1500 C. or below should exceed 30,000 p.s.i. tangential compressive stress has been obtained in pyrolytic carbon coatings between about 5000 and 30,000 p.s.i. with the resultant coated articles exhibiting high structural strengths. Tangential compressive stress at least as high as 20,000 p.s.i., may be obtained using a substrate made of graphite to which the pyrolytic carbn forms an excellent bond. An actual upper limit of the tangential compressive strength has not been determined and will presumably be dependent at least in part upon the substrate material and how strong a bond is obtained thereto. In general when this upper limit is exceeded, if the carbon layer is relatively thick, debonding occurs, and if the carbon coating is thin, compressive failure of the carbon layer occurs.
Articles of various geometric configurations may be coated in accordance with the present invention. Usually the coated articles will have a largest dimension at least equal to one-half inch inasmuch as the strength of the article is a desired advantage. However, for some specific purposes, smaller articles might be desirable. Spheres, rods and even tubes are examples of such articles that may be fabricated having good structural strength.
The following examples show two illustrative processes for making strong articles coated with pyrolytic carbon.
Both examples employ the generally preferred methods of depositing isotropic carbon at temperatures below about 1500 C. For purpose of further explanation, when employing a pyrolytic deposition process, it is generally not substantially more difiicult to deposit isotropic carbon at temperatures below about 1500 C. than to deposit laminar carbon or higher temperature isotropic carbon. Accordingly, because such lower temperature isotropic carbons can be deposited having a BAF of 1.1 or less, apparent crystallite sizes of 50 A. or less and a density up to about 2.0 g./cm. they are usually employed because they have greater strength and greater wearability. However, isotropic carbon deposited at temperatures above about 1500 C., as from methane or propane or the like, might be used for many applications. Likewise, Laminar carbon, which as deposited from methane at temperatures below 1500 C. has a apparent crystallite size of about 50 A. or less and has a density greater or equal to about 1.5 g./cc., may adequately fill the requirements of many applications.
EXAMPLE I A generally spherical article is chosen made of graphite having a coelficient of thermal expansion of about 8Xl0- C. The spheroid, approximately inch in diameter, is lightly sandblasted to remove any loose particles and is placed in a vertical graphite reaction tube. The tube is about 6.3 centimeters in diameter and is heated to a temperature of about vl400 C. while a how of helium gas therethrough is maintainend. When coating is ready to begin, the spheroid plus an ancillary charge of grams of zirconium dioxide particles (to provide additional available deposition surface area as explained in UJS. Pat. 3,399,969) having an average particle size of about 400 microns are loaded into the reaction tube. Propane gas is admixed with the helium to provide a partial pressure of propane of about 0.3 atm. (total pressure of 1 atm.). The total flow of gas is held at about 4000 cc. per minute. The propane undergoes pyrolysis and deposits carbon, Carbon is deposited on the spheroid in the form of isotropic pyrolytic carbon having a coefficient of thermal expansion of about 5X l0- C. Subsequent examination also shows the carbon has a BAF of about 1.1, an apparent crystallite size of about 40 A. and a density of about 1.7 grams per cm. Deposition is continued until an isotropic pyrolytic carbon coating about 6 mils microns) thick is obtained, a time of about an hour.
The resultant coated sphere is allowed to cool to ambient temperature and is removed from the reaction tube. The change in temperature of nearly 1400 C. between the deposition temperature and ambient temperature effects a sufiiciently greater contraction of the substrate carbon spheroid than of the isotropic car-bon coating to set up a circumferential compressive stress in the coating of about 15,000 p.s.i. This stress is well below the estimated compressive fracture stress of the coating.
.The resultant coated article is considered to have high structural strength. For example, a control article which is similarly coated with pyrolytic isotropic carbon which has a greater coefficient of thermal expansion than the carbon substrate, so that its circumference is under tensile strength, will fracture upon being dropped from a height of about three feet. The coated article described above having its outer coating in compressive stress may be dropped repeatedly from the same height Without damage. Other tests show the coated spheroid exhibits not only good resistance to fracture, but also good wearresistance.
EXAMPIJE II A graphite spheroid similar to that coated in Example I is introduced into the same reaction tube which is heated to a temperature of about 1350 C. while maintaining 21 flow of helium gas through it. When coating is ready to begin, a similar ancillary charge of 100 grams of Zr particles is loaded into the reaction tube. Propane gas is admixed with the helium to provide a gas flow of about 8000 cc. per minute having a partial pressure of propane of about 0.4 atm. (total pressure of 1 atm.). All of the helium is bubbled through methyltrichlorosilane. The propane and the methyltrichlorosilane pyrolyze to deposit a mixture of isotropic carbon and silicon carbide on the spheroid. Deposition is continued until a coating about 8 mils (200 microns) thick is obtained, a time of about an hour.
The resultant coated sphere is allowed to cool to ambient temperature and is removed from the reaction tube. Examination of the isotropic carbon-silicon carbide coating shows it has a coefiicient of thermal expansion of about 6 10 C. and a density of about 2 grams per cmfi. The coating contains about .10 weight percent silicon, in the form of silicon carbide. The isotropic carbon has a BAF of about 1.1 and an apparent crystallite size of about 35 A. The change in temperature effects a sufliciently greater contraction of the substrate spheroid than of the coating to set up a circumferential compressive stress in the coating of about 10,000 p.s.i. This stress is well below the estimated compressive fracture stress of the coating.
The resultant coated article is considered to have excellent structural strength. The coated spheroid may be dropped repeatedly from about three feet without damage. Other tests show the coated spheroid exhibits not only good resistance to fracture, but also good wearresistance. The isotropic carbon-silicon carbide coating is considered to have all the advantages from the standpoint of strength and wearability as the completely carbon coating produced in Example I. Moreover, with other coating variables being maintained generally equal, it is considered that an isotropic carbon coating that is deposited with a silicon carbide additive will have greater strength than the same isotropic carbon without the additive. In general, it is considered that up to about 15 percent by weight of silicon, or an equivalent amount of a similar carbide-forming additive, may be included without detracting from the desirable properties of the pyrolytic carbon coatings as described hereinbefore.
Various modifications and alternative embodiments of the present invention will be suggested to those having skill in the art and are intended to be within the spirit and scope of the present invention.
Various of the features of the present invention are set forth in the following claims.
What is claimed is:
1. A coated article having high strength characteristics, which comprises an article made of graphite having a coefficient of thermal expansion between 6 to 9 X 10- C. and a coating of pyrolytic carbon surrounding said graphite article which pyrolytic carbon was deposited thereupon at a temperature well above ambient and which has a strong bond to said underlying graphite article, said pyrolytic carbon having a density of at least 1.5 -g./ cc. and having a coefficient of thermal expansion which is less than that of the graphite article and being under substantial compressive tangential stress as a result of the thermal contraction occurring during cooling the coated graphite article from deposition temperature to ambient temperature.
2. The coated article in accordance with claim 1 where- 6 in said compressive tangential stress is at least about 5000 p.s.i.
3. The coated article in accordance with claim 1 wherein the thickness of said pyrolytic carbon coating is at least about 25 microns.
4. The coated article in accordance with claim 1 whereing said pyrolytic carbon is isotropic carbon.
5. The coated article in accordance with claim 4 wherein said isotropic carbon has an apparent crystallite size of about 50 A. or less.
.6. The coated article in accordance with claim 5 wherein said isotropic carbon has a BAiF of about 1.1 or less.
7. The coated article in accordance with claim 1 wherein said pyrolytic carbon coating contains an additive carbide dispersed therethroughout.
8. The coated article in accordance with claim 7 wherein said additive carbide is silicon carbide.
9. A method of forming an article having high strength characteristics, which method comprises heating a graphite article having a coefficient of thermal expansion between 6 and 9X 10-/ C. to a preselected deposition temperature of at least about 1200 C., effecting deposition of pyrolytic carbon on said graphite article from a carbonaceous atmosphere at said preselected temperature under conditions that result in formulation of carbon having a density of at least 1.5 g./cc. and having a coefficient of thermal expansion which is less than that of said graphite article, and cooling the coated graphite article to ambient temperature, the difierence between the coefiicients of expansion of said graphite article and of said pyrolytic carbon being such and the bond therebetween being sufliciently strong that in cooling from deposition temperature to ambient temperature said pyrolytic carbon coating is placed under substantial compressive tangential stress.
10. A method in accordance with claim 9 wherein said deposition temperature is not greater than about 15 00 C.
11. A method in accordance with claim 9 wherein the compressive tangential stress is at least about 5000 p.s.i.
12. A method in accordance with claim 9 wherein the thickness of said pyrolytic carbon coating is at least about 25 microns.
13. A method in accordance with claim 9 wherein said carbonaceous atmosphere contains a hydrocarbon, an inert gas and a volatile compound containing a carbide-forming element.
14. A method in accordance with claim 13 wherein said volatile compound contains silicon.
15. A method in accordance with claim 9 wherein said pyrolytic carbon coating is isotropic carbon having an apparent crystallite size of about 50 A. or less.
References Cited UNITED STATES PATENTS 3,167, 449 11/1965 Spacil 117-46 CG X 3,399,969 9/ 1968 Bokros et al 117-226 X 3,379,555 4/1968 Hough 117-46 3,471,314 10/ 1969 Beatty et a1 117-46 3,472,677 10/1969 Beutlen et al. 117-46 3,369,920 2/ 1968 Bourdeau et al. 117-46 CG 3,526,005 9/ 1970 Bokros et al. 117-46 CG EDWARD G. WHITBY, Primary Examiner U.S. Cl. X.R.
23-2091; ll7-l2l, 135.1, A, Dig. 6; 264-29
US764954A 1968-10-03 1968-10-03 Coated article and method for making same Expired - Lifetime US3676179A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US76495468A 1968-10-03 1968-10-03

Publications (1)

Publication Number Publication Date
US3676179A true US3676179A (en) 1972-07-11

Family

ID=25072262

Family Applications (1)

Application Number Title Priority Date Filing Date
US764954A Expired - Lifetime US3676179A (en) 1968-10-03 1968-10-03 Coated article and method for making same

Country Status (6)

Country Link
US (1) US3676179A (en)
CH (1) CH539688A (en)
DE (1) DE1950066C3 (en)
FR (1) FR2019796A1 (en)
GB (1) GB1277498A (en)
SE (1) SE356737B (en)

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3969130A (en) * 1973-02-05 1976-07-13 General Atomic Company Carbon-coated articles and method of making same
US4128680A (en) * 1977-06-03 1978-12-05 Honeywell Inc. Silicon coated ceramic substrate with improvements for making electrical contact to the interface surface of the silicon
US4145250A (en) * 1976-02-26 1979-03-20 General Atomic Company In situ regeneration of the first wall of a deuterium-tritium fusion device
US4226914A (en) * 1978-05-19 1980-10-07 Ford Motor Company Novel spraying composition, method of applying the same and article produced thereby
US4288495A (en) * 1978-05-19 1981-09-08 Ford Motor Company Article coated with beta silicon carbide and silicon
US4343658A (en) * 1980-04-14 1982-08-10 Exxon Research & Engineering Co. Inhibition of carbon accumulation on metal surfaces
US4529626A (en) * 1984-07-27 1985-07-16 Exxon Research And Engineering Co. Inhibition of carbon accumulation on metal surfaces
US5084151A (en) * 1985-11-26 1992-01-28 Sorin Biomedica S.P.A. Method and apparatus for forming prosthetic device having a biocompatible carbon film thereon
US5370684A (en) * 1986-12-12 1994-12-06 Sorin Biomedica S.P.A. Prosthesis of polymeric material coated with biocompatible carbon
US5387247A (en) * 1983-10-25 1995-02-07 Sorin Biomedia S.P.A. Prosthetic device having a biocompatible carbon film thereon and a method of and apparatus for forming such device
US5514410A (en) * 1994-09-08 1996-05-07 Carbon Implants, Inc. Pyrocarbon and process for depositing pyrocarbon coatings
US6596084B1 (en) 1999-05-20 2003-07-22 Medicalcv, Inc. Pyrolytic carbon coating apparatus having feed gas actuator
US6777029B2 (en) 2002-04-27 2004-08-17 Carbomedics Inc. Method for determining product coating rates for fluidized beds
US20050065600A1 (en) * 2003-09-19 2005-03-24 Mhatre Harischandra K. Prosthetic heart valve of pyrolytic carbon
US20160002774A1 (en) * 2014-07-03 2016-01-07 Solarcity Corporation Wafer carrier for reducing contamination from carbon particles and outgassing
US10074755B2 (en) 2013-01-11 2018-09-11 Tesla, Inc. High efficiency solar panel
US10084099B2 (en) 2009-11-12 2018-09-25 Tesla, Inc. Aluminum grid as backside conductor on epitaxial silicon thin film solar cells
US10084107B2 (en) 2010-06-09 2018-09-25 Tesla, Inc. Transparent conducting oxide for photovoltaic devices
US10115838B2 (en) 2016-04-19 2018-10-30 Tesla, Inc. Photovoltaic structures with interlocking busbars
US10115839B2 (en) 2013-01-11 2018-10-30 Tesla, Inc. Module fabrication of solar cells with low resistivity electrodes
US10164127B2 (en) 2013-01-11 2018-12-25 Tesla, Inc. Module fabrication of solar cells with low resistivity electrodes
US10181536B2 (en) 2015-10-22 2019-01-15 Tesla, Inc. System and method for manufacturing photovoltaic structures with a metal seed layer
US10610925B2 (en) 2014-09-15 2020-04-07 Schunk Kohlenstofftechnik Gmbh Casting mold and methods for production
US10672919B2 (en) 2017-09-19 2020-06-02 Tesla, Inc. Moisture-resistant solar cells for solar roof tiles
US11190128B2 (en) 2018-02-27 2021-11-30 Tesla, Inc. Parallel-connected solar roof tile modules

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0722018B2 (en) * 1988-03-04 1995-03-08 シャープ株式会社 Method of manufacturing graphite electrode
FR2677740B1 (en) * 1991-06-11 1998-03-13 Europ Propulsion LOADING DEVICE FOR SUPPORTING PARTS INSIDE AN OVEN.

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3969130A (en) * 1973-02-05 1976-07-13 General Atomic Company Carbon-coated articles and method of making same
US4145250A (en) * 1976-02-26 1979-03-20 General Atomic Company In situ regeneration of the first wall of a deuterium-tritium fusion device
US4128680A (en) * 1977-06-03 1978-12-05 Honeywell Inc. Silicon coated ceramic substrate with improvements for making electrical contact to the interface surface of the silicon
US4226914A (en) * 1978-05-19 1980-10-07 Ford Motor Company Novel spraying composition, method of applying the same and article produced thereby
US4288495A (en) * 1978-05-19 1981-09-08 Ford Motor Company Article coated with beta silicon carbide and silicon
US4343658A (en) * 1980-04-14 1982-08-10 Exxon Research & Engineering Co. Inhibition of carbon accumulation on metal surfaces
US5387247A (en) * 1983-10-25 1995-02-07 Sorin Biomedia S.P.A. Prosthetic device having a biocompatible carbon film thereon and a method of and apparatus for forming such device
US4529626A (en) * 1984-07-27 1985-07-16 Exxon Research And Engineering Co. Inhibition of carbon accumulation on metal surfaces
US5084151A (en) * 1985-11-26 1992-01-28 Sorin Biomedica S.P.A. Method and apparatus for forming prosthetic device having a biocompatible carbon film thereon
US5370684A (en) * 1986-12-12 1994-12-06 Sorin Biomedica S.P.A. Prosthesis of polymeric material coated with biocompatible carbon
US5514410A (en) * 1994-09-08 1996-05-07 Carbon Implants, Inc. Pyrocarbon and process for depositing pyrocarbon coatings
US5677061A (en) * 1994-09-08 1997-10-14 Medtronic Carbon Implants, Inc. Pyrocarbon and process for depositing pyrocarbon coatings
US6596084B1 (en) 1999-05-20 2003-07-22 Medicalcv, Inc. Pyrolytic carbon coating apparatus having feed gas actuator
US6777029B2 (en) 2002-04-27 2004-08-17 Carbomedics Inc. Method for determining product coating rates for fluidized beds
US20050065600A1 (en) * 2003-09-19 2005-03-24 Mhatre Harischandra K. Prosthetic heart valve of pyrolytic carbon
US10084099B2 (en) 2009-11-12 2018-09-25 Tesla, Inc. Aluminum grid as backside conductor on epitaxial silicon thin film solar cells
US10084107B2 (en) 2010-06-09 2018-09-25 Tesla, Inc. Transparent conducting oxide for photovoltaic devices
US10074755B2 (en) 2013-01-11 2018-09-11 Tesla, Inc. High efficiency solar panel
US10115839B2 (en) 2013-01-11 2018-10-30 Tesla, Inc. Module fabrication of solar cells with low resistivity electrodes
US10164127B2 (en) 2013-01-11 2018-12-25 Tesla, Inc. Module fabrication of solar cells with low resistivity electrodes
US10309012B2 (en) * 2014-07-03 2019-06-04 Tesla, Inc. Wafer carrier for reducing contamination from carbon particles and outgassing
US20160002774A1 (en) * 2014-07-03 2016-01-07 Solarcity Corporation Wafer carrier for reducing contamination from carbon particles and outgassing
US10610925B2 (en) 2014-09-15 2020-04-07 Schunk Kohlenstofftechnik Gmbh Casting mold and methods for production
US10181536B2 (en) 2015-10-22 2019-01-15 Tesla, Inc. System and method for manufacturing photovoltaic structures with a metal seed layer
US10115838B2 (en) 2016-04-19 2018-10-30 Tesla, Inc. Photovoltaic structures with interlocking busbars
US10672919B2 (en) 2017-09-19 2020-06-02 Tesla, Inc. Moisture-resistant solar cells for solar roof tiles
US11190128B2 (en) 2018-02-27 2021-11-30 Tesla, Inc. Parallel-connected solar roof tile modules

Also Published As

Publication number Publication date
FR2019796A1 (en) 1970-07-10
DE1950066A1 (en) 1970-04-09
GB1277498A (en) 1972-06-14
DE1950066C3 (en) 1976-01-08
DE1950066B2 (en) 1975-05-15
SE356737B (en) 1973-06-04
CH539688A (en) 1973-07-31

Similar Documents

Publication Publication Date Title
US3676179A (en) Coated article and method for making same
US3969130A (en) Carbon-coated articles and method of making same
US3264073A (en) Novel metal microspheres and their manufacture
US3095316A (en) Process for coating carbonaceous articles with silicon dioxide
US3547676A (en) Pyrolytic carbon structures and process for making same
CA1136863A (en) Integral composite of polycrystalline diamond and/or cubic boron nitride body phase and substrate phase
US4242106A (en) Composite of polycrystalline diamond and/or cubic boron nitride body/silicon carbide substrate
US4425407A (en) CVD SiC pretreatment for carbon-carbon composites
US3399969A (en) Deposition of massive pyrolytic carbon
US5614140A (en) Methods for fabricating diamond film and solid fiber composite structure
US4585704A (en) Electrically conductive Si3 N4 --C series amorphous material and a method of processing the same
US2972556A (en) Composite coated carbonaceous article and process of making the same
US3949106A (en) Method for producing isotropic pyrolisis carbon coatings
CN105813975A (en) Carbon composites, methods of manufacture, and uses thereof
GB1433216A (en) Composite structures comprising isotropic graphite members
US4353953A (en) Integral composite of polycrystalline diamond and/or cubic boron nitride body phase and substrate phase
US3464843A (en) Pyrolytic graphite alloys and method of making the same
US4225355A (en) Amorphous boron-carbon alloy in bulk form and methods of making the same
JPH0365527A (en) Silicon oxicarbide glass and its article
US3900675A (en) Rocket nozzle comprising pyrolytic graphite-silicon carbide microcomposite inserts
Cahn et al. Newer forms of carbon and their uses
US2996783A (en) Method of shaping sic by vaporization and condensation
US3925133A (en) Method for making reinforced pyrolytic graphite-silicon carbide microcomposites
US3799790A (en) Metal carbide spherules encapsulated within a pyrolytic carbon shell
US3247008A (en) Process for coating radioactive spheroids with pyrolytic graphite

Legal Events

Date Code Title Description
AS Assignment

Owner name: GA TECHNOLOGIES INC 10955 JOHN JAY HOPKINS DR. P.

Free format text: ASSIGNS ENTIRE INTEREST. SUBJECT TO REORGANIZATION AGREEMENT DATED JUNE 14, 1982;ASSIGNOR:GENERAL ATOMIC COMPANY;REEL/FRAME:004081/0313

Effective date: 19821029

AS Assignment

Owner name: GENERAL ATOMICS

Free format text: CHANGE OF NAME;ASSIGNOR:GA TECHNOLOGIES, INC.,;REEL/FRAME:004914/0588

Effective date: 19880201