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US3977896A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for depositing pyrolytic carbon coatings

Assignee: General Atomics Corp
•
Filing: 1972-03-09
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Granted: 1976-08-31
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Expires: 1992-03-09
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Abstract

Abstract Fluidized bed process for coating materials with pyrolytic carbon. A gaseous atmosphere including a carbonaceous substance is flowed upward through a vertical heated enclosure to fluidize a bed of particles therein. An exit conduit extends into the particle bed and a controlled flow of inert gas is fed through the conduit to regulate the exit passage of particles from the bed. Additional particles are added to the bed from above.

Inventors

  • 👤 Jack C. Bokros
  • 👤 Robert J. Akins, Sr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 17:23
CPC Classifications
C; C23; C23C; C23C24/00; B; B01; B01J; B01J2/00; B01J2/003; C01; C01B; C01B32/00; C04; C04B; C04B35/00; C04B35/515; C04B35/52; C23C16/00; C23C16/22; C23C16/26; C23C16/44; C23C16/442; Y; Y10; Y10T; Y10T428/00; Y10T428/23907; Y10T428/23921

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 196 words
In a process for depositing pyrolytic carbon coatings, which process includes disposing particles less than a millimeter in size and having an initial density of at least about 3 gm/cm 3 in a fluidized bed coating enclosure, flowing an atmosphere containing a carbonaceous substance through the enclosure while heating the particles to a temperature sufficient to cause thermal decomposition of said substance and deposition of pyrolytic carbon coatings, the improvement which comprises removing from the coating enclosure controlled numbers of particles which have grown in size as a result of said carbon deposition, said removal being carried out by gravity flow through withdrawal conduit means from the upper one-third of said fluidized bed and without disrupting said flow of said atmosphere through said enclosure, the rate at which said particles are removed from said enclosure being controlled by regulating the rate of flow of an inert gas stream which flows upward through the conduit means to create resistance to said gravity removal of said particles, and adding to the coating enclosure particles of smaller size in an amount proportional to said removed particles to maintain the total deposition surface area within the coating enclosure relatively constant.
Claim 2
Dependent Claim 196 words
In a process for depositing pyrolytic carbon coatings, which process includes disposing particles less than a millimeter in size and having an initial density of at least about 3 gm/cm 3 in a fluidized bed coating enclosure, flowing an atmosphere containing a carbonaceous substance through the enclosure while heating the particles to a temperature sufficient to cause thermal decomposition of said substance and deposition of pyrolytic carbon coatings, the improvement which comprises removing from the coating enclosure controlled numbers of particles which have grown in size as a result of said carbon deposition, said removal being carried out by gravity flow through withdrawal conduit means from the upper one-third of said fluidized bed and without disrupting said flow of said atmosphere through said enclosure, the rate at which said particles are removed from said enclosure being controlled by regulating the rate of flow of an inert gas stream which flows upward through the conduit means to create resistance to said gravity removal of said particles, and adding to the coating enclosure particles of smaller size in an amount proportional to said removed particles to maintain the total deposition surface area within the coating enclosure relatively constant.
Claim 3
Dependent Claim 76 words
The improved process in accordance with claim 1 wherein a fluidized bed of particles is established by passing a stream of gas upward therethrough, wherein the ratio of the total deposition surface area, measured in sq. cm., to the void volume thereof, measured in cu. cm., is at least about 2 to 1, and wherein the temperature of said particles is maintained at at least about 1200°C. and a mixture of helium and propane is employed.
Claim 4
Dependent Claim 22 words
The improved process in accordance with claim 1 wherein a layer of pyrolytic carbon at least about 150 microns thick is deposited.
Claim 5
Dependent Claim 59 words
The improved process in accordance with claim 1 wherein isotropic pyrolytic carbon is deposited and wherein the ratio of the total deposition surface area, measured in square centimeters, in the active region of the enclosure wherein deposition occurs, to the void volume, measured in cubic centimeters, of said active region is maintained at at least about 2 to 1.
Claim 6
Dependent Claim 23 words
The improved process in accordance with claim 4 wherein said ratio is maintained at a value not greater than about 20 to 1.
Claim 7
Dependent Claim 16 words
The improved process in accordance with claim 4 wherein said hydrocarbon is either propane or propylene.
Claim 8
Dependent Claim 19 words
The improved process in accordance with claim 4 wherein said atmosphere contains a carbonaceous substance plus an inert gas.
Claim 9
Dependent Claim 52 words
The improved process in accordance with claim 7 wherein the contact time of said atmosphere in the fluidized bed coater is between about 0.1 sec. and about 0.3 sec., said temperature is between about 1200°C. and 1400°C. and said carbonaceous substance is a hydrocarbon with molecular weight between about 20 and 75.
Claim 10
Dependent Claim 31 words
The improved process in accordance with claim 4 wherein at least one object having a dimension greater than about 5 millimeters is included in said enclosure for coating with pyrolytic carbon.
Claim 11
Dependent Claim 25 words
The improved process in accordance with claim 9 wherein the average size of said initial particles is between about 50 microns and about 600 microns.

References Cited (Backward Citations)

US2414625A Cited
US2719779A Cited
US3399969A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-08-31 1980-03-01 1980-08-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-08-31 1984-03-01 1984-08-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-08-31 1988-03-01 1988-08-31 $7700.00 Window Closed / Lapsed

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