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US4182783A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of vapor deposition

Assignee: PPG Industries Inc
•
Filing: 1977-09-23
•
Granted: 1980-01-08
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Expires: 1997-09-23
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Abstract

Abstract An apparatus and method are provided for fluidizing and vaporizing particulate solid coating reactants by first establishing a fluidized bed of dispersed particulant solid coating reactants and thereafter drawing a volume of fluidizing gas and suspended particulate solid coating reactant to a vaporizer while mixing an additional volume of gas therewith and then vaporizing the dispersed particulate solid coating reactant in the reactant-gas mixture. The reactant-gas mixture is then directed into contact with a hot substrate to be coated in order to deposit a film thereon.

Inventors

  • 👤 Vern A. Henery

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 00:25
CPC Classifications
C; C23; C23C; C23C16/00; C23C16/44; C23C16/448; C23C16/4481; C23C16/453; Y; Y10; Y10S; Y10S118/00; Y10S118/05

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 173 words
In a method of coating a substrate with a film by deposition from a reactant composition wherein the reactant composition is caused to react at a surface of the substrate by maintaining the substrate at a temperature sufficient to cause pyrolysis of the reactant composition upon its contact therewith, the improvement which comprises fluidizing a mass of particulate solid coating reactant with a gas at a temperature substantially below the reaction temperature, decomposition temperature or vaporization temperature of the reactant; drawing a volume of fluidizing gas and suspended particulate solid reactant from the fluidized mass as a particulate reactant-gas composition; mixing the withdrawn volume of particulate reactant-gas composition with an additional volume of gas to dilute the particulate reactant-gas composition while maintaining the temperature of the mixture below the reaction temperature, decomposition temperature or vaporization temperature of the reactant; and directing the mixture against a substrate dispersing the solid reactant over a surface of it while maintaining the substrate at a sufficient temperature to cause the solid reactant to react depositing a film.
Claim 2
Dependent Claim 173 words
In a method of coating a substrate with a film by deposition from a reactant composition wherein the reactant composition is caused to react at a surface of the substrate by maintaining the substrate at a temperature sufficient to cause pyrolysis of the reactant composition upon its contact therewith, the improvement which comprises fluidizing a mass of particulate solid coating reactant with a gas at a temperature substantially below the reaction temperature, decomposition temperature or vaporization temperature of the reactant; drawing a volume of fluidizing gas and suspended particulate solid reactant from the fluidized mass as a particulate reactant-gas composition; mixing the withdrawn volume of particulate reactant-gas composition with an additional volume of gas to dilute the particulate reactant-gas composition while maintaining the temperature of the mixture below the reaction temperature, decomposition temperature or vaporization temperature of the reactant; and directing the mixture against a substrate dispersing the solid reactant over a surface of it while maintaining the substrate at a sufficient temperature to cause the solid reactant to react depositing a film.
Claim 3
Dependent Claim 42 words
The method according to claim 1 wherein the particulate reactant-gas mixture is maintained at a temperature below about 120° F. (50° C.) prior to directing it against a substrate and maintaining the substrate at a temperature above about 400° F. (205° C.).
Claim 4
Dependent Claim 56 words
The method according to claim 2 wherein the particulate reactant-gas mixture is maintained at a temperature of from about 60° F. to 80° F. (15° C. to 25° C.) prior to directing it against a substrate and the substrate is maintained at a temperature from about 1000° C. to 1300° F. (540° C. to 705° C.).
Claim 5
Dependent Claim 35 words
The method according to claim 1, wherein the diluted particulate reactant-gas composition is heated to a temperature above the vaporization temperature of the reactant prior to directing the composition against a substrate to be coated.
Claim 6
Dependent Claim 27 words
The method according to claim 4, wherein the temperature of the diluting gas is sufficiently greater than the temperature of the fluidizing gas to accomplish said heating.
Claim 7
Dependent Claim 22 words
The method according to claim 4 wherein said heating is accomplished by introducing the diluted particulate reactant-gas composition into a heating chamber.
Claim 8
Dependent Claim 21 words
The method according to claim 4, wherein the diluted particulate reactant-gas composition is heated by further dilution with a hot gas.
Claim 9
Dependent Claim 31 words
The method according to claim 7 wherein the composition is further heated to a desired temperature for contacting the substrate to be coated by conveying the composition through a heating zone.
Claim 10
Dependent Claim 28 words
The method according to claim 4 wherein the reactant-gas composition and diluting gas are introduced into a heating chamber under conditions to establish turbulence within the heating chamber.
Claim 11
Dependent Claim 25 words
The method according to claim 1 wherein a volume of fluidizing gas and particulate reactant is mixed with 3 to 20 volumes of diluting gas.
Claim 12
Dependent Claim 69 words
The method according to claim 1 wherein said volume of fluidizing gas and fluidized particulate reactant is drawn from the fluidized mass through a vacuum ejector and the additional volume of diluting gas is introduced into the vacuum ejector under pressure in a sufficient volume to establish a vacuum therein causing the volume of fluidizing gas and fluidized particulate reactant to be drawn into and through the vacuum ejector.

References Cited (Backward Citations)

US2780553A Cited
US3198167A Cited
US3852098A Cited
US3970037A Cited
US3786309A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-01-07 1983-07-09 1984-01-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-01-07 1987-07-09 1988-01-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-01-07 1991-07-09 1992-01-08 $7700.00 Window Closed / Lapsed

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