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US2955966A - Manufacture of semiconductor material - Google Patents

Manufacture of semiconductor material Download PDF

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US2955966A
US2955966A US741327A US74132758A US2955966A US 2955966 A US2955966 A US 2955966A US 741327 A US741327 A US 741327A US 74132758 A US74132758 A US 74132758A US 2955966 A US2955966 A US 2955966A
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conductor
silicon
semi
hydride
manufacture
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US741327A
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Sterling Henley Frank
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International Standard Electric Corp
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International Standard Electric Corp
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    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B11/00Single-crystal growth by normal freezing or freezing under temperature gradient, e.g. Bridgman-Stockbarger method
    • C30B11/04Single-crystal growth by normal freezing or freezing under temperature gradient, e.g. Bridgman-Stockbarger method adding crystallising materials or reactants forming it in situ to the melt
    • C30B11/08Single-crystal growth by normal freezing or freezing under temperature gradient, e.g. Bridgman-Stockbarger method adding crystallising materials or reactants forming it in situ to the melt every component of the crystal composition being added during the crystallisation
    • C30B11/12Vaporous components, e.g. vapour-liquid-solid-growth
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/02Silicon
    • C01B33/021Preparation
    • C01B33/027Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material
    • C01B33/029Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material by decomposition of monosilane
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00Boron; Compounds thereof
    • C01B35/02Boron; Borides
    • C01B35/023Boron
    • 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
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S117/00Single-crystal, oriented-crystal, and epitaxy growth processes; non-coating apparatus therefor
    • Y10S117/912Replenishing liquid precursor, other than a moving zone
    • 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
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S420/00Alloys or metallic compositions
    • Y10S420/903Semiconductive
    • 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
    • Y10T117/00Single-crystal, oriented-crystal, and epitaxy growth processes; non-coating apparatus therefor
    • Y10T117/10Apparatus
    • Y10T117/1024Apparatus for crystallization from liquid or supercritical state

Definitions

  • the monocrystal is in the form of a rod and there are some limitations upon the diameter of the monocrystalline rod produced either by this method or by the previously known method of pulling from a melt in a crucible.
  • the method according to the present invention involves the decomposition of a hydride of the semi-conductor material that can be obtained free from contamination by compounds of impurity elements.
  • a gaseous hydride of the semi-conductor element is passed through a zone in which it is decomposed by means of electro-magnetic energy applied to the gas. On leaving this zone, association of some of the atoms in the said gaseous compound takes place with the liberation of energy, which is sufficient to melt the semi-conductor material.
  • the outer conductor 1 of a coaxial transmission line 1, 2 for high frequency electromagnetic energy is sealed through the upper closure plate 3 for a cylinder 4 of silica.
  • the coaxial transmission line 1, 2 is preferably made of silver and the inner conductor 2 consists of a hollow tube. Water is circulated through the inner conductor 2 by means of an inlet pipe 5 extending down the interior of hollow conductor 2 and an outlet pipe 6 branched from conductor 2 near the end thereof remote from the end In order to avoid contamination of inlet pipe 5.
  • the end of inner conductor 2 which protrudes through plate 3 is closed as shown to allow of such water circulation.
  • The'inner and outer conductors 1, 2 are held in spaced relation by washers 7, 8 of polytetrafluorethylene.
  • the Washer 7 seals the space between inner and outer conductors 1 and 2 except for a'pipe 9 through which silane gas enters the space between inner and outer conductors, whilst the washer 8 is provided with orifices throughwhich silane gas can pass.
  • Radio frequency power is supplied to the coaxial transmission line 1, 2 from a generator, shown diagrammatically at 10 connected between inner and outer conductors 11, 12 of a feeder coaxial transmission line connected to the line 1, 2 one quarter wave length from that end of the line 1, 2 closed by the washer 7.
  • This power may be of a frequency between /2 mc./s. and 1000 mc./s., preferably between 500 and 1000 mc./s.
  • a suitable power is 5 kw.
  • the length of the transmission line is made such that thefirst voltage anti-node occurs at or near that end of the transmission line 1, 2 that is within the cylinder 4.
  • a rod 13 of silicon is mounted on a support 14 that is sealed through a bottom closure plate 15 for the cylinder 4 in such a manner that it is capable of longitudinal movement.
  • Gearing 16 is provided for effecting such movement.
  • a protective gas such as argon enters the cylinder 4 through inlet pipe 17 and leaves through outlet pipe 18.
  • the silane which flows through the space between inner and outer conductors is decomposed at the anti-node of the coaxial transmission line into silicon and atomic hydrogen.
  • the atoms of hydrogen recombine into molecules with evolution of heat, forming an'electrodeless flame discharge 19 which melts the silicon resulting from the decomposition of the silane.
  • the rod 13 is placed so that its upper end is in the region of the discharge and is melted thereby to form a pool 20 ofmolten silicon.
  • the silicon resulting from this decomposition is deposited on this molten pool.
  • the rod 13 is gradually lowered andthe silicon previously deposited solidifies.
  • the silicon mounted on the support 14 is shown as a rod 13 it is to be understood that this is the condition after the process has been in operation for some time. Initially only a seed of silicon is mounted on support 14. If this seed be a monocrystal the rod 13 may be grown as a monocrystal by suitable regulation of its rate of growth. By means of the apparatus and method described it is possible to grow a rod of monocrystalline silicon having a diameter in excess of 2.5 cm. and the growth rate is greater than can be achieved by the method according to British Patent No. 745,698 and is as great as can be achieved by a crystal pulling technique.
  • Thevessel 4 is filled withargon which provides a protective atmosphere preventing oxidation of the growing crystal.
  • the invention is applicable to the manufacture of any semi-conductor elements having volatile hydrides such as silicon, germanium, boron &c.
  • semi-conductor element is meant an element which is (a) semi-conductive when alone or (b) will produce a semi-conductive material when in combination with another element.
  • the hydride may be used in the same manner as silane in the manufacture of silicon.
  • Boron, phosphorus, arsenic and/or antimony may be used to confer on silicon or germanium semiconductor properties of a particular type N or P and are, therefore, preferably manufactured as thin layers in a monocrystal of silicon or germanium.
  • N- type germanium or silicon is produced by replacing silane in the example above quoted by a mixture in suitable proportions of silane and diborane, or a mixture of germanium hydride and diborane. The flow of the mixture through the high frequency field is continued only for suflicient length of time to produce the required amount of N-type material.
  • N and P type material or of N, intrinsic and P type material may be produced in this manner throughout the body of semi-conductor monocrystal grown.
  • the temperature produced in the flame may be reduced by mixing a monatomic gas such as argon with the gaseous hydride, and thus reducing the degree of disassociation and subsequent re-association that takes place.
  • a monatomic gas such as argon
  • the flow of argon through the cylinder 4 may be regulated.
  • the gaseous hydride such as silane used in this process may be mixed with hydrogen if it be found necessary to slow down the rate of production of the solid semi-conductor material without reducing the temperature in the flame, and thus in this case a mixture of hydrogen and silane is fed through pipe 9.
  • Method of manufacturing a semi-conductor element which comprises flowing a gaseous hydride of said element past a voltage anti-node in an electrical high frequency transmission line whereby the hydride is decomposed into the element and atomic hydrogen, melting the semi-conductor material by heat produced by the recombination of hydrogen atoms resulting from such decomposition and collecting the molten element.
  • the said high frequency transmission line is a coaxial transmission line having separated outer and inner conductors which comprises feeding said line with electromagnetic energy of a frequency between /2 mc./s. and 1000 mc./s., terminating said line near a voltage anti-node, flowing said gaseous hydride through the space between said inner and outer conductors, and collecting the molten element 4 upon a seed body within the flame produced by the said recombination of atoms of hydrogen.
  • Method as claimed in claim 3 comprising also the step of withdrawing the said seed body with the deposited molten material at a rate commensurate with the rate of deposition of molten material.
  • Method of manufacturing a monocrystalline body of an element chosen from the class consisting of silicon and germanium which comprises. decomposing a gaseous hydride of said element at a voltage node of a high frequency electrical transmissionline supplied with suitable electrical power, melting the semiconductor material by heat produced by the recombination of hydro-gen atoms resulting from such decomposition, depositing the molten semiconductor element upon a monocrystalline seed of the same element and withdrawing the seed with the deposited material from the molten zone to allow solidification of the molten material as a monocrystal.
  • Apparatus for manufacturing a body of semi-conductor element chosen from the class consisting of silicon and germanium comprising a coaxial electric transmission line having an outer conductor and a hollow inner conductor, means for circulating cooling fluid through said inner conductor, means for applying electrical energy of a frequency between /2 mc./s. and 1000 mc./s.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
  • Silicon Compounds (AREA)

Description

Oct. 11, 1960 H. F. STERLING MANUFACTURE OF SEMICONDUCTOR MATERIAL Filed June 11, 1958 I n ventor A ttorne y MANUFACTURE OF SEMICONDUCTOR MATERIAL Henley Frank Sterling, London, England, assignor to International Standard Electric Corporation, New York, N.Y., a corporation of Delaware Filed June 11, 1958, Ser. No. 741,327
Claims priority, application Great Britain July 3, 1957 States Patent centration substantially less than normal into a zone a heated to a temperature at least equal to the decomposition temperature of silane. This method of. manufacture has proved successful in producing silicon of such a high degree of purity, that no impurities are detectable spectrographically. Monocrystalline silicon can be produced by this process but the rate of growth of a body of such silicon is slow so that it is preferred to produce at a faster rate a polycrystalline body which is afterwards converted into a monocrystal by melting and pulling a crystal from the melt. from a crucible it is preferred to pull the monocrystal by means of the method and apparatus described in U.S. application No. 688,460, filed October 7, 1957.
The monocrystal is in the form of a rod and there are some limitations upon the diameter of the monocrystalline rod produced either by this method or by the previously known method of pulling from a melt in a crucible.
In British Patent No. 778,383, it has been proposed to manufacture other semi-conductor material, such as germanium, by thermal decomposition of the corresponding hydride.
It is the object of the present invention to manufacture semi-conductor material of a very high degree of purity at a faster rate than that achieved by the methods above referred to.
The method according to the present invention involves the decomposition of a hydride of the semi-conductor material that can be obtained free from contamination by compounds of impurity elements.
According to the present invention a gaseous hydride of the semi-conductor element is passed through a zone in which it is decomposed by means of electro-magnetic energy applied to the gas. On leaving this zone, association of some of the atoms in the said gaseous compound takes place with the liberation of energy, which is sufficient to melt the semi-conductor material.
The invention will be better understood from the following description of one form of apparatus for carrying out the invention, taken in conjunction with the accompanying drawing.
Referring to the drawing, there is shown in section an apparatus for the manufacture of pure silicon. The outer conductor 1 of a coaxial transmission line 1, 2 for high frequency electromagnetic energy is sealed through the upper closure plate 3 for a cylinder 4 of silica. The coaxial transmission line 1, 2 is preferably made of silver and the inner conductor 2 consists of a hollow tube. Water is circulated through the inner conductor 2 by means of an inlet pipe 5 extending down the interior of hollow conductor 2 and an outlet pipe 6 branched from conductor 2 near the end thereof remote from the end In order to avoid contamination of inlet pipe 5. The end of inner conductor 2 which protrudes through plate 3 is closed as shown to allow of such water circulation. The'inner and outer conductors 1, 2 are held in spaced relation by washers 7, 8 of polytetrafluorethylene. The Washer 7 seals the space between inner and outer conductors 1 and 2 except for a'pipe 9 through which silane gas enters the space between inner and outer conductors, whilst the washer 8 is provided with orifices throughwhich silane gas can pass.
Radio frequency power is supplied to the coaxial transmission line 1, 2 from a generator, shown diagrammatically at 10 connected between inner and outer conductors 11, 12 of a feeder coaxial transmission line connected to the line 1, 2 one quarter wave length from that end of the line 1, 2 closed by the washer 7. This power may be of a frequency between /2 mc./s. and 1000 mc./s., preferably between 500 and 1000 mc./s. A suitable power is 5 kw. The length of the transmission line is made such that thefirst voltage anti-node occurs at or near that end of the transmission line 1, 2 that is within the cylinder 4. w
A rod 13 of silicon is mounted on a support 14 that is sealed through a bottom closure plate 15 for the cylinder 4 in such a manner that it is capable of longitudinal movement. Gearing 16 is provided for effecting such movement. A protective gas such as argon enters the cylinder 4 through inlet pipe 17 and leaves through outlet pipe 18. v
In operation the silane which flows through the space between inner and outer conductors is decomposed at the anti-node of the coaxial transmission line into silicon and atomic hydrogen. Immediately beyond this point the atoms of hydrogen recombine into molecules with evolution of heat, forming an'electrodeless flame discharge 19 which melts the silicon resulting from the decomposition of the silane. The rod 13 is placed so that its upper end is in the region of the discharge and is melted thereby to form a pool 20 ofmolten silicon. The silicon resulting from this decomposition is deposited on this molten pool. As further silicon is deposited the rod 13 is gradually lowered andthe silicon previously deposited solidifies.
Although the silicon mounted on the support 14 is shown as a rod 13 it is to be understood that this is the condition after the process has been in operation for some time. Initially only a seed of silicon is mounted on support 14. If this seed be a monocrystal the rod 13 may be grown as a monocrystal by suitable regulation of its rate of growth. By means of the apparatus and method described it is possible to grow a rod of monocrystalline silicon having a diameter in excess of 2.5 cm. and the growth rate is greater than can be achieved by the method according to British Patent No. 745,698 and is as great as can be achieved by a crystal pulling technique.
Thevessel 4 is filled withargon which provides a protective atmosphere preventing oxidation of the growing crystal. i
The invention is applicable to the manufacture of any semi-conductor elements having volatile hydrides such as silicon, germanium, boron &c. By semi-conductor element is meant an element which is (a) semi-conductive when alone or (b) will produce a semi-conductive material when in combination with another element.
For the manufacture of germanium the hydride may be used in the same manner as silane in the manufacture of silicon. Boron, phosphorus, arsenic and/or antimony may be used to confer on silicon or germanium semiconductor properties of a particular type N or P and are, therefore, preferably manufactured as thin layers in a monocrystal of silicon or germanium. For example N- type germanium or silicon is produced by replacing silane in the example above quoted by a mixture in suitable proportions of silane and diborane, or a mixture of germanium hydride and diborane. The flow of the mixture through the high frequency field is continued only for suflicient length of time to produce the required amount of N-type material. This flow is then succeeded by a flow of silane or germane as the case may be if intrinsic silicon or germanium is. to be produced, why a flow of silane or germane mixed in the required proportion with phosphine, if P-type material is to be produced.
Successive layers of N and P type material or of N, intrinsic and P type material may be produced in this manner throughout the body of semi-conductor monocrystal grown.
In any process according to the invention the temperature produced in the flame may be reduced by mixing a monatomic gas such as argon with the gaseous hydride, and thus reducing the degree of disassociation and subsequent re-association that takes place. For this purpose the flow of argon through the cylinder 4 may be regulated.
Mixture of another gas with the gaseous hydride re duces the amount of semi-conductor solid produced for a given volume of gas, and a reduction of the amount of semi-conductor solid produced may be necessary, in the case of production of mono-crystalline material, to ensure a rate of growth compatible with the production of a single crystal.
The gaseous hydride such as silane used in this process may be mixed with hydrogen if it be found necessary to slow down the rate of production of the solid semi-conductor material without reducing the temperature in the flame, and thus in this case a mixture of hydrogen and silane is fed through pipe 9.
Any such added hydrogen must be in pure condition to avoid any possible introduction of impurities into the semi-conductor material.
While the principles of the invention have been described above in connection with specific embodiments, and particular modifications thereof, it is to be clearly understood that this description is made only by way of example and not as a limitation on the scope of the invention.
What I claim is:
1. Method of manufacturing a semi-conductor element which comprises flowing a gaseous hydride of said element past a voltage anti-node in an electrical high frequency transmission line whereby the hydride is decomposed into the element and atomic hydrogen, melting the semi-conductor material by heat produced by the recombination of hydrogen atoms resulting from such decomposition and collecting the molten element.
2. Method as claimed in claim 1 in which the semiconductor element is silicon.
3. Method as claimed in claim 1 in which the said high frequency transmission line is a coaxial transmission line having separated outer and inner conductors which comprises feeding said line with electromagnetic energy of a frequency between /2 mc./s. and 1000 mc./s., terminating said line near a voltage anti-node, flowing said gaseous hydride through the space between said inner and outer conductors, and collecting the molten element 4 upon a seed body within the flame produced by the said recombination of atoms of hydrogen.
4. Method as claimed in claim 3 comprising also the step of withdrawing the said seed body with the deposited molten material at a rate commensurate with the rate of deposition of molten material.
5. Method as claimed in claim 4 in which said seed body is a monocrystal.
6. Method of manufacturing a monocrystalline body of an element chosen from the class consisting of silicon and germanium which comprises. decomposing a gaseous hydride of said element at a voltage node of a high frequency electrical transmissionline supplied with suitable electrical power, melting the semiconductor material by heat produced by the recombination of hydro-gen atoms resulting from such decomposition, depositing the molten semiconductor element upon a monocrystalline seed of the same element and withdrawing the seed with the deposited material from the molten zone to allow solidification of the molten material as a monocrystal.
7. Method as claimed in claim 6 of manufacturing a monocrystalline body having successive N and P regions therein which comprisesv successively mixing the hydride of the said element with hydrides of donor and acceptor elements.
8. Apparatus for manufacturing a body of semi-conductor element chosen from the class consisting of silicon and germanium comprising a coaxial electric transmission line having an outer conductor and a hollow inner conductor, means for circulating cooling fluid through said inner conductor, means for applying electrical energy of a frequency between /2 mc./s. and 1000 mc./s. and of suitable power between said inner and outer conductor, means for flowing a hydride of the said semiconductor element through the space between said inner and outer conductors, said conductors being terminated near to a voltage anti-nodal position for said energy, means for locating a seed body at such distance from the said anti-nodal position as to be within the flame produced by recombination of atoms beyond said position, and means for moving said seed body away from said position.
9. Apparatus as claimed in claim 8 in which said antinodal position is within a vessel through a wall of which said outer conductor is sealed and means for passing a monatomic gas into and out of said vessel.
References Cited in the file of this patent UNITED STATES PATENTS 2,313,028 Siegmann Mar. 2, 1943 2,541,697 Glassbrook Feb. 13, 1951 2,684,329 Rouy July 20, 1954 2,768,074 Stauffer Oct. 23, 1956 OTHER REFERENCES Comptes Rendus, vol. 89, page 1069, published in 1879.
Comptus Rendus, vol. 138, pages 1169 and 1170, published in 1904.

Claims (1)

1. METHOD OF MANUFACTURING A SEMI-CONDUCTOR ELEMENT WHICH COMPRISES FLOWING A GASEOUS HYDRIDE OF SAID ELEMENT PAST A VOLTAGE ANTI-NODE IN AN ELECTRICAL HIGH FREQUENCY TRANSMISSION LINE WHEREBY THE HYDRIDE IS DECOMPOSED INTO THE ELEMENT AND ATOMIC HYDROGEN, MELTING THE SEMI-CONDUCTOR MATERIAL BY HEAT PRODUCED BY THE RECOMBINATION OF HYDROGEN ATOMS RESULTING FROM SUCH DECOMPOSITION AND COLLECTING THE MOLTEN ELEMENT.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3170859A (en) * 1959-03-25 1965-02-23 Merck & Co Inc Process for the preparation of silicon films
US3173814A (en) * 1962-01-24 1965-03-16 Motorola Inc Method of controlled doping in an epitaxial vapor deposition process using a diluentgas
US4102764A (en) * 1976-12-29 1978-07-25 Westinghouse Electric Corp. High purity silicon production by arc heater reduction of silicon intermediates
US4102765A (en) * 1977-01-06 1978-07-25 Westinghouse Electric Corp. Arc heater production of silicon involving alkali or alkaline-earth metals
US4102767A (en) * 1977-04-14 1978-07-25 Westinghouse Electric Corp. Arc heater method for the production of single crystal silicon

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2313028A (en) * 1939-05-04 1943-03-02 Siegmann Friedrich Process for the production of sodium and potassium hydride
US2541697A (en) * 1946-10-03 1951-02-13 Socony Vacuum Oil Co Inc Electronic reactor
US2684329A (en) * 1951-07-07 1954-07-20 L L H Company Method and apparatus for promoting chemical reaction
US2768074A (en) * 1949-09-24 1956-10-23 Nat Res Corp Method of producing metals by decomposition of halides

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2313028A (en) * 1939-05-04 1943-03-02 Siegmann Friedrich Process for the production of sodium and potassium hydride
US2541697A (en) * 1946-10-03 1951-02-13 Socony Vacuum Oil Co Inc Electronic reactor
US2768074A (en) * 1949-09-24 1956-10-23 Nat Res Corp Method of producing metals by decomposition of halides
US2684329A (en) * 1951-07-07 1954-07-20 L L H Company Method and apparatus for promoting chemical reaction

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3170859A (en) * 1959-03-25 1965-02-23 Merck & Co Inc Process for the preparation of silicon films
US3173814A (en) * 1962-01-24 1965-03-16 Motorola Inc Method of controlled doping in an epitaxial vapor deposition process using a diluentgas
US4102764A (en) * 1976-12-29 1978-07-25 Westinghouse Electric Corp. High purity silicon production by arc heater reduction of silicon intermediates
US4102765A (en) * 1977-01-06 1978-07-25 Westinghouse Electric Corp. Arc heater production of silicon involving alkali or alkaline-earth metals
US4102767A (en) * 1977-04-14 1978-07-25 Westinghouse Electric Corp. Arc heater method for the production of single crystal silicon

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