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US4289801A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for producing fine grained pyrolytic silicon nitride

Assignee: RTX Corp
•
Filing: 1980-05-21
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Granted: 1981-09-15
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Expires: 2000-05-21
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Abstract

Abstract Novel fine grained pyrolytic silicon nitride is produced by adding a substantial amount of methane to the normal reactant gases. Silicon tetrafluoride and ammonia in ratios of 60:40 to 10:90 may be employed with additions of methane in amounts equal to from 50 to 500% of the sum of silicon tetrafluoride and ammonia. When these reactant gases are passed over a heated substrate at a low pressure pyrolytic silicon nitride with a grain size of less than about 10 microns results.

Inventors

  • 👤 Francis S. Galasso
  • 👤 Malcolm Basche, deceased

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 20:58
CPC Classifications
C; C23; C23C; C23C16/00; C23C16/22; C23C16/30; C23C16/34; C23C16/345

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 112 words
A method for producing fine grain pyrolytic silicon nitride which comprises: providing reactant gases which comprise from 40 to 90% ammonia, balance silicon halide and an amount of methane equal to from about 50 to 500% of the reactant gases, mixing these gases and flowing them into a reaction chamber which contains a substrate, said reaction chamber and substrate being heated to from 1200° to 1900° C. and said reaction chamber being maintained at a partial pressure of less than 300 mm of Hg of reactant gases, so that fine grained pyrolytic silicon nitride free of carbon and having a grain size less than about 10 microns is deposited on the substrate.
Claim 2
Independent Claim 112 words
A method for producing fine grain pyrolytic silicon nitride which comprises: providing reactant gases which comprise from 40 to 90% ammonia, balance silicon halide and an amount of methane equal to from about 50 to 500% of the reactant gases, mixing these gases and flowing them into a reaction chamber which contains a substrate, said reaction chamber and substrate being heated to from 1200° to 1900° C. and said reaction chamber being maintained at a partial pressure of less than 300 mm of Hg of reactant gases, so that fine grained pyrolytic silicon nitride free of carbon and having a grain size less than about 10 microns is deposited on the substrate.
Claim 3
Dependent Claim 24 words
A method as in claim 1 wherein the ammonia is present in an amount equal to from 50 to 85% of the reactant gases.
Claim 4
Dependent Claim 23 words
A method as in claim 1 wherein the methane is added in amounts of from about 150 to 400% of the reactant gases.
Claim 5
Dependent Claim 20 words
A method as in claim 1 wherein the reaction chamber and substrate temperature is held between 1200° and 1600° C.
Claim 6
Dependent Claim 22 words
A method as in claim 1 wherein the reaction chamber partial pressure of reactant gases is less than 100 mm of Hg.
Claim 7
Dependent Claim 23 words
A method as in claim 1 wherein the reaction chamber partial pressure of reactant gas is from 1 to 10 mm of Hg.

References Cited (Backward Citations)

US3211527A Cited
US3226194A Cited
US3565674A Cited
US3637423A Cited
US4036653A Cited
US4091169A Cited
US4118539A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-09-14 1985-03-16 1985-09-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-09-14 1989-03-16 1989-09-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-09-14 1993-03-16 1993-09-15 $7700.00 Window Closed / Lapsed

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