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US4488914A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the epitaxial deposition of III-V compounds utilizing a continuous in-situ hydrogen chloride etch

Assignee: United States Department of the Air Force
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Filing: 1982-10-29
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Granted: 1984-12-18
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Expires: 2002-10-29
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Abstract

Abstract A process for depositing an epitaxial film of a III-V compound onto the surface of a crystallographically compatible substrate which includes contacting said substrate with a vaporous mixture of a group III element and a group V element to effect the deposition of a group III-V compound thereon while simultaneously introducing a flow of hydrogen halide gas during deposition of the group III-V compound.

Inventors

  • 👤 Kenneth P. Quinlan
  • 👤 Thomas E. Erstfeld

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 15:26
CPC Classifications
H; H10; H10P; H10P14/00; H10P14/20; H10P14/29; H10P14/2901; H10P14/24; H10P14/2907; H10P14/2909; H10P14/34; H10P14/3402; H10P14/3414; H10P14/3418; H10P14/36

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 313 words
A method for preparing and depositing an epitaxial film consisting essentially of indium phosphide onto the surface of a suitable substrate crystallographically compatible with said film, said method consisting essentially of the steps of: (A) positioning a substrate suitable for epitaxial growth of indium phosphide on the surface thereof in a first deposition zone located at one end of a quartz reaction chamber while maintaining said first deposition zone at a predetermined temperature; (B) positioning a source material consisting essentially of indium in a second source zone located at the other end of said quartz chamber while maintaining said second source zone at a predetermined temperature; (C) introducing a gaseous mixture consisting essentially of (a) a first hydrogen chloride gas and (b) a hydrogen carrier gas into said second source zone and passing said gaseous mixture over said indium source to produce a first gaseous reactant consisting essentially of indium chloride; (D) introducing said first gaseous indium chloride reactant into a third mixing zone of said quartz chamber, said third mixing zone being maintained at a predetermined temperature and positioned intermediate said first deposition and said second source zones; (E) introducing a second gaseous reactant into said third mixing zone simultaneously with the entry of said first gaseous reactant into said third mixing zone, said second gaseous reactant comprising a mixture of (a) phosphine and (b) a hydrogen carrier gas to form a gaseous mixture consisting essentially of indium chloride, phosphine and hydrogen; (F) continously introducing a flow of a second hydrogen chloride gas into said third mixing zone to form a gaseous admixture consisting essentially of (a) said second hydrogen cloride gas and (b) said gaseous mixture of indium chloride, phosphine and hydrogen and subsequently introducing said formed gaseous admixture into said heated first deposition zone to contact said substrate and affect the deposition of an indium phosphide, epitaxial, crystalline film thereon.
Claim 2
Independent Claim 313 words
A method for preparing and depositing an epitaxial film consisting essentially of indium phosphide onto the surface of a suitable substrate crystallographically compatible with said film, said method consisting essentially of the steps of: (A) positioning a substrate suitable for epitaxial growth of indium phosphide on the surface thereof in a first deposition zone located at one end of a quartz reaction chamber while maintaining said first deposition zone at a predetermined temperature; (B) positioning a source material consisting essentially of indium in a second source zone located at the other end of said quartz chamber while maintaining said second source zone at a predetermined temperature; (C) introducing a gaseous mixture consisting essentially of (a) a first hydrogen chloride gas and (b) a hydrogen carrier gas into said second source zone and passing said gaseous mixture over said indium source to produce a first gaseous reactant consisting essentially of indium chloride; (D) introducing said first gaseous indium chloride reactant into a third mixing zone of said quartz chamber, said third mixing zone being maintained at a predetermined temperature and positioned intermediate said first deposition and said second source zones; (E) introducing a second gaseous reactant into said third mixing zone simultaneously with the entry of said first gaseous reactant into said third mixing zone, said second gaseous reactant comprising a mixture of (a) phosphine and (b) a hydrogen carrier gas to form a gaseous mixture consisting essentially of indium chloride, phosphine and hydrogen; (F) continously introducing a flow of a second hydrogen chloride gas into said third mixing zone to form a gaseous admixture consisting essentially of (a) said second hydrogen cloride gas and (b) said gaseous mixture of indium chloride, phosphine and hydrogen and subsequently introducing said formed gaseous admixture into said heated first deposition zone to contact said substrate and affect the deposition of an indium phosphide, epitaxial, crystalline film thereon.
Claim 3
Dependent Claim 21 words
A method in accordance with claim 1 wherein said second hydrogen halide gas is first combined with said second gaseous reactant.
Claim 4
Dependent Claim 21 words
A method in accordance with claim 1 wherein said second hydrogen halide gas is introduced directly into said heated third zone.
Claim 5
Dependent Claim 38 words
A method in accordance with claim 1 wherein said substrate consists essentially of an iron-doped indium phosphide compound and said first, second and third zones are maintained at temperatures of about 650° C., 900° C. and 950°, respectively.
Claim 6
Dependent Claim 67 words
A method in accordance with claim 1 wherein said phosphine is introduced at a flow rate of about 2.3 to 15.9 cc/minute; said first hydrogen chloride is introduced at a flow rate of about 5.3 cc/minute; said second hydrogen chloride is introduced at a flow rate of about 0.1 to 1.5 cc/minute and said inert gases are introduced at a total flow rate of about 1680 cc/minute.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-12-18 1988-06-18 1988-12-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-12-18 1992-06-18 1992-12-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-12-18 1996-06-18 1996-12-18 $7700.00 Window Closed / Lapsed

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