US3796548A - Boat structure in an apparatus for making semiconductor compound single crystals - Google Patents

Boat structure in an apparatus for making semiconductor compound single crystals Download PDF

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US3796548A
US3796548A US00180041A US3796548DA US3796548A US 3796548 A US3796548 A US 3796548A US 00180041 A US00180041 A US 00180041A US 3796548D A US3796548D A US 3796548DA US 3796548 A US3796548 A US 3796548A
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seed
crystal
growth
boat
section
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D Boss
E Hull
S Scilla
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International Business Machines 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
    • C30B11/14Single-crystal growth by normal freezing or freezing under temperature gradient, e.g. Bridgman-Stockbarger method characterised by the seed, e.g. its crystallographic orientation
    • 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
    • C30B11/003Heating or cooling of the melt or the crystallised material
    • 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
    • Y10S117/90Apparatus characterized by composition or treatment thereof, e.g. surface finish, surface coating
    • 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
    • Y10T117/1092Shape defined by a solid member other than seed or product [e.g., Bridgman-Stockbarger]

Definitions

  • ABSTRACT An apparatus useful for growing single crystal semiconductor material comprising a'liquid melt section coaxially integrated with a seed cavity and having an annularly disposed integral thermal reflector means and a radiant heat dissipating member horizontally disposed and in a post linear directionfrom the seed cavity.
  • This invention relates to apparatus for making single crystal semiconductor compounds and especially relates to a method and apparatus for the preparation of Group III-V single crystal compounds such as gallium arsenide ingots and slices thereof, suitable for use as semiconductor structures.
  • Doped and undoped single semiconductor crystals have been prepared or grown by a large variety of techniques. The most common involves the progressive, directional solidification of a molten semiconductor material from a starting seed crystal. The liquid is usually contained in a boat in .contact with said single crystal seed. The solid liquid interface is moved away from the seed by motion of the boat movement of the tempera-v ture gradient profile, or'by pulling the seed from the melt. These methodsare often referred to as the I-Iorizontal Bridgman, Gradient Freeze and the Czochralski techniques.
  • the boat containing the molten charge and a seed crystal of the desired orientation is situated in this gradient such that the point in the gradient corresponding to the melting temperature of the crystal is located at the pointatwhich the solid-liquid interface is desired during the seeding of the melt. Relative motion of the boat with respect to the gradient results in directional freezing of the crystal.
  • the melt is usually comprised of a molten compound of the approximate stoichiometry of the crystal to be grown as a single crystal.
  • the melt is usually held at a temperature above the melting point of the compound under an atmosphere of the more volatile elementat a pressure approximately equal to the dissociation pressure of the compound at its melting point.
  • Prior structures utilized in single crystal horizontal .growth did not maintain thermal symmetry about the crystal growth axis which hampered the desired and normal growth direction of the crystal along the horizontal axis of the boat. This condition nucleates unpredicted deviations from the normal growth axis which in turn voids the control of the geometry of the slice taken from the boule or ingot or results in polycrystalline growth,
  • these prior structures could not maintain the orientation of the seed crystal with respect to the longitudinal axis of theboat. This also affects the crystalline characteristics and geometry of slices taken from boules or ingots grown in these structures.
  • Seed cavities having a rectangular shape do not allow freedom of movement of the seed in' response to mechanical stress resulting from thermal .discontinuities surrounding the melt.
  • the seed becomes keyed in as a result of seed cavity wall distortions which results in stress being placed on the growing crystal due to differential thermal expansion.
  • Another object of this invention is to provide an apparatus for the monocrystalline growth of semiconductor material whereby the resultant boule or ingot is of such nature as to provide maximum control of the geometry of slices 'cut therefrom.
  • a monocrystalline semiconductor growth apparatus adaptable to providing a sharp temperature gradient at the solid-liquid interface of the crystal growth process and providing means for axially dissipating radiant heat energy from the hot to the cold segments of the process furnace and heating apparatus.
  • FIG. 1 is a perspective view of a boat apparatus for the growth of single crystal material showing a semicylindrical liquid containing section and an adjacent coaxial semi-conical section adjacent to said liquid containing section and the semi-cylindrical seed section or cavity with its associated radiant heat pipe and reflec-
  • FIG. 2 is a cross-sectional fragmented view of the crystal growing apparatus contained in a sealed tube which in turn is enclosed in a multizone furnace.
  • FIG. 3 is a cross-sectional fragmented view of the monocrystalline growing apparatus showing the liquid solid seed interface with the heat shield and the radiant heat dissipating member.
  • FIG. 4 is a fragmented top plan view showing the solid-liquid interface contained in the crystal growing apparatus and the associated heat shield and radiant energy conducting means.
  • FIG. 1 illustrates a specific configuration of the single crystal semiconductor crystal growing apparatus.
  • the apparatus is constructed of clear fused silica having a sand-blasted or roughened surface which avoids wetting of the interior surface by the molten liquid material.
  • the illustrative configuration of the liquid containing or melt section 1 is connected by a semi-conical coaxial transition section 2 to a coaxial semi-cylindrical seed containing section 3 of smaller radius than the melt section 1.
  • An integral tilted reflection member 4 annularly surrounding the seed cavity 3 near the center of seed 5 is provided.
  • Said reflecting means redirects radial heat flow from and about the conical coaxial section 2 backward and toward said section 2 illustrated in FIG. 4 by arrows 11; thereby preventing radial heat losses from the said conical section.
  • the resultant temperature stabilization prevents localized cold spots which produce polycrystalline nucleation which decreases the ultimate quality of the single crystal boule which in turn decreases yield.
  • the radiant energy conducting means 6 is a solid. cylinder of clean smooth and non-sandblasted fused silica having flame polished ends. This cylinder or light pipe conducts radiant energy longitudinally along the axis of the apparatus toward a colder furnace section subsequently explained and illustrated in reference to FIG. 2.
  • the apparatus constructed as illustrated and utilized in the process of single semiconductor crystal growth creates a radial thermal symmetry which enhances crystal growth along the horizontal axis of the apparatus without significant deviation therefrom.
  • FIG. 2 illustrates the crystal growing apparatus contained in a closed tube 7 which is in turn contained in a double or dual zone furnace arrangement whereby the hot'zone is maintained at a temperature to keep the molten material at 8 in a molten condition and sustains a solid liquid interface at 9 between the-molten polycrystalline material 8 and the solid seed 5.
  • the solid-liquid interface at 9 is maintained in a slightly convex configuration in the direction of the molten material.
  • This solid-liquid interface configuration results from the relatively higher horizontal heat flow with respect to the radial heat flow through the longitudinal heat conducting member 6 and illustrated by the arrows ll) in FIG. 4.
  • the interface configuration is concave toward the molten charge and detrimental to the growth of crystals with a high degree of perfection.
  • the single crystal growth apparatus of this invention is further described in connection with its application to the well known process for making doped or undoped gallium arsenide and known as the Horizontal Bridgman technique.
  • stoichiometric quantities of gallium and arsenic are reacted in a closedtube which is subjected to a temperature gradient of approximately 614 to 1,240C.
  • a double furnace apparatus as shown in FIG. 2 is provided having a cold zone 12 and a hot zone 13 and separated by an insulating partition 14.
  • a stoichiometric amount of polycrystalline gallium is placed in the liquid melt section 1 of the apparatus with a given amount of the desired dopant.
  • a previously prepared seed of the desired crystallographic orientation is inserted into the seed cavity.
  • the apparatus containing the aforesaid materials is placed in a tube with a sufficient amount of arsenic to maintain the stoichiometry of the melt plus an excess to maintain a condensed phase at one atmosphere of pressure at about 614C.
  • a seal off plug is inserted into the tube and the tube evacuated to 10" Torr, whereupon the tube is conventionally sealed off by collapsing the tube onto the plug.
  • the tube is now inserted into the furnace and brought to thermal equilibrium and positioned so that the gallium and dopant material are located in the hot section of the furnace and maintained in a molten state.
  • the liquid solid interface between the molten polycrystalline gallium and the seed crystal is located at a temperature of about 1,240C in the thermal gradient.
  • the tube is then moved at the desired crystal growth rate and with respect to the furnace from the hot zone toward the colder zone while maintaining the solidliquid interface between the molten gallium arsenide and the seed crystal within the said 1,240C temperature zone. This results in a horizontal directional freezing or crystallization of the charge.
  • the tube Upon completion of the crystallization of the molten charge, the tube is allowed to slowly cool to room temperature, whereby thermal shock is avoided, whereupon the tube is broken open and the apparatus containing the gallium arsenide ingot is removed.
  • the ingot or boule thus formed is preserved for further processing.
  • An apparatus for growing monocrystalline semiconductor material comprising a primary concave-boat section adapted to contain a melt and an integral concave end section having a decreased depth and width relative to said concave primary boat section and adapted to hold a seed crystal contacting said melt, the primary and end sections disposed axially, said end section having a disc shaped radiant heat reflecting means angularly and annularly disposed to the boat axis and a heat dissipating means secured in the distal portion of said end section and extending externally thereof and forming an end section closure.

Abstract

An apparatus useful for growing single crystal semiconductor material comprising a liquid melt section coaxially integrated with a seed cavity and having an annularly disposed integral thermal reflector means and a radiant heat dissipating member horizontally disposed and in a post linear direction from the seed cavity.

Description

United States Batent 1191 Boss et a1.
[ BOAT STRUCTURE IN AN APPARATUS FOR MAKING SEMICONDUCTOR COMPOUND SINGLE CRYSTALS [75] Inventors: David W. Boss, Beacon; Edward M.
Hull, La Gtangeville; Salvatore J. Scilla, Marlboro, all of N.Y.
[73] 'Assignee: International Business Machines Corporation, Armonk, N.Y.
22 Filed: Sept. 13,1971 21' Appl. No.2 180,041-
[52] us. 61. 23/273 SP, 23/301 SP [51] Int. Cl B01j 17/06 [58'] 'Field-of Search 23/273 SP, 301 SP [56] References Cited UNITED STATES PATENTS 3,124,489 3 1964 Vogel et al. 23/273 3,156,533 11/1964 lmber 1 23/273 I 3,198,606 8/1965 Lyons .1 23/301 3,210,165 10/1965 .Van Run 6161. 23/301 1451 Mar. 112, 1974 3,453,352 7/1969 Goundry .L 23/27'3 3,464,812 9/1969 Utech et a1. 23/301 3,607,054 9/1971 Conrad i 23/273 3,617,223 11/1971 Boatman 23/273 3,240,568 3/1966 Derby et a1. 23/301 3,172,734 3/1965 Warren 23/301 3,520,810 7/1970 Plaskett et aL 23/301 3,401,022 9/1968 Marshall et al....' 23/301 Primary Examiner-Norman Yudkoff Assistant Examiner-R. T. Foster Attorney, Agent, or Firm'Danie1 E. lgo; Wesley DeBruin [5 7] ABSTRACT An apparatus useful for growing single crystal semiconductor material comprising a'liquid melt section coaxially integrated with a seed cavity and having an annularly disposed integral thermal reflector means and a radiant heat dissipating member horizontally disposed and in a post linear directionfrom the seed cavity.
3 Claims, 4 Drawing Figures 5 7 COOL ZONE COOL ZONE HOT ZONE PATENTEDMAR 12 1914 INVENTORS DAVID w. BOSS EDWARD M. HULL SALVATOR SCILLA ##z: BY
FIELD OF THE INVENTION This invention relates to apparatus for making single crystal semiconductor compounds and especially relates to a method and apparatus for the preparation of Group III-V single crystal compounds such as gallium arsenide ingots and slices thereof, suitable for use as semiconductor structures.
BACKGROUND OF THE INVENTION Doped and undoped single semiconductor crystals have been prepared or grown by a large variety of techniques. The most common involves the progressive, directional solidification of a molten semiconductor material from a starting seed crystal. The liquid is usually contained in a boat in .contact with said single crystal seed. The solid liquid interface is moved away from the seed by motion of the boat movement of the tempera-v ture gradient profile, or'by pulling the seed from the melt. These methodsare often referred to as the I-Iorizontal Bridgman, Gradient Freeze and the Czochralski techniques.
In the Horizontal Bridgman method, crystals are grown in a sealed fused silica system infused silica boats. The fused silica boat surfaces are usually sandblasted to produce a multi-faceted or disrupted surface in order to prevent wetting and avoid sticking or adhering of the produced material to the boat surface. Syn-, thesis is usually performed from the elements in situ prior to growth. Usually, a two-zone furnace is employed to furnish two independently controllable temperature zones, one of which is at a higher temperature than the other. The hotter zone is controlled at a temperature above the melting point of the crystal to be grown. A thermal gradient of known characteristics is maintained at one end of this furnace. In'practice, the boat containing the molten charge and a seed crystal of the desired orientation is situated in this gradient such that the point in the gradient corresponding to the melting temperature of the crystal is located at the pointatwhich the solid-liquid interface is desired during the seeding of the melt. Relative motion of the boat with respect to the gradient results in directional freezing of the crystal.
The melt is usually comprised of a molten compound of the approximate stoichiometry of the crystal to be grown as a single crystal. The melt is usually held at a temperature above the melting point of the compound under an atmosphere of the more volatile elementat a pressure approximately equal to the dissociation pressure of the compound at its melting point. T. S. Plaskett, et al., J. Electrochemical Society, Solid State Science, January 1971, pp. 1 -1 17, describes the concept in relation to the production of gallium arsenide;
The prior art has taught certain boat structures hav' ing seed cavities associated with semi-cylindrical sec produce a solid-liquid interface, the movement of which from a higher to a lower temperature produces a single crystal ingot conforming in part to the configuration of the vessel.
Subsequently, it was found desirable to incorporate a separate seed cavity adjacent to and associated with the liquid containing cavity in an attempt to obtain a proper neckdown of the growing seed crystal and to facilitate the growth of larger single crystal ingots from smaller seed crystals.
Prior structures utilized in single crystal horizontal .growth did not maintain thermal symmetry about the crystal growth axis which hampered the desired and normal growth direction of the crystal along the horizontal axis of the boat. This condition nucleates unpredicted deviations from the normal growth axis which in turn voids the control of the geometry of the slice taken from the boule or ingot or results in polycrystalline growth, In addition, these prior structures could not maintain the orientation of the seed crystal with respect to the longitudinal axis of theboat. This also affects the crystalline characteristics and geometry of slices taken from boules or ingots grown in these structures.
Seed cavities having a rectangular shape do not allow freedom of movement of the seed in' response to mechanical stress resulting from thermal .discontinuities surrounding the melt. The seed becomes keyed in as a result of seed cavity wall distortions which results in stress being placed on the growing crystal due to differential thermal expansion.
The random or radial heat loss from the area surrounding the liquid-solid interface results in spurious growth and an undesirable twinning condition in the crystal growth process. Similarly, said heat loss causes localized polycrystalline growth which grossly deteriorates the yield of crystal growth. A I
US. Pat. No. 3,520,810 relating to a process for the productionof gallium arsenide illustrates the prior art apparatus having the disadvantages recited heretofore.
SUMMARY OF THE INVENTION It is an object of this invention to provide an appara tus for the horizontal growth of doped or undoped single crystals adaptable for use as semiconductor structures.
It is a further object of this invention to provide an apparatus for the horizontal growth of single crystal semiconductor materials wherein the direction of the crystal growth is along the horizontal axis of the growth vessel without significant deviation therefrom.
It is still a further object of this invention to provide a semiconductor single crystal growth apparatus having a seed cavity adaptable to utilizing minimum seed material.
Another object of this invention is to provide an apparatus for the monocrystalline growth of semiconductor material whereby the resultant boule or ingot is of such nature as to provide maximum control of the geometry of slices 'cut therefrom.
The aforesaid and other objects are accomplished by providing a monocrystalline semiconductor growth apparatus adaptable to providing a sharp temperature gradient at the solid-liquid interface of the crystal growth process and providing means for axially dissipating radiant heat energy from the hot to the cold segments of the process furnace and heating apparatus.
The foregoing and other objects, features and advantages of the invention and the accomplishment thereof will be apparent from the following more particular description of preferred embodiments of the invention as illustrated in the accompanying drawing and examples.
DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view of a boat apparatus for the growth of single crystal material showing a semicylindrical liquid containing section and an adjacent coaxial semi-conical section adjacent to said liquid containing section and the semi-cylindrical seed section or cavity with its associated radiant heat pipe and reflec- FIG. 2 is a cross-sectional fragmented view of the crystal growing apparatus contained in a sealed tube which in turn is enclosed in a multizone furnace.
FIG. 3 is a cross-sectional fragmented view of the monocrystalline growing apparatus showing the liquid solid seed interface with the heat shield and the radiant heat dissipating member.
FIG. 4 is a fragmented top plan view showing the solid-liquid interface contained in the crystal growing apparatus and the associated heat shield and radiant energy conducting means.
DESCRIPTION OF THE PREFERRED EMBODIMENT Referring to the drawings, FIG. 1 illustrates a specific configuration of the single crystal semiconductor crystal growing apparatus. Typically, the apparatus is constructed of clear fused silica having a sand-blasted or roughened surface which avoids wetting of the interior surface by the molten liquid material. The illustrative configuration of the liquid containing or melt section 1 is connected by a semi-conical coaxial transition section 2 to a coaxial semi-cylindrical seed containing section 3 of smaller radius than the melt section 1.
An integral tilted reflection member 4 annularly surrounding the seed cavity 3 near the center of seed 5 is provided. Said reflecting means redirects radial heat flow from and about the conical coaxial section 2 backward and toward said section 2 illustrated in FIG. 4 by arrows 11; thereby preventing radial heat losses from the said conical section. The resultant temperature stabilization prevents localized cold spots which produce polycrystalline nucleation which decreases the ultimate quality of the single crystal boule which in turn decreases yield.
The radiant energy conducting means 6 is a solid. cylinder of clean smooth and non-sandblasted fused silica having flame polished ends. This cylinder or light pipe conducts radiant energy longitudinally along the axis of the apparatus toward a colder furnace section subsequently explained and illustrated in reference to FIG. 2. The apparatus constructed as illustrated and utilized in the process of single semiconductor crystal growth creates a radial thermal symmetry which enhances crystal growth along the horizontal axis of the apparatus without significant deviation therefrom.
FIG. 2 illustrates the crystal growing apparatus contained in a closed tube 7 which is in turn contained in a double or dual zone furnace arrangement whereby the hot'zone is maintained at a temperature to keep the molten material at 8 in a molten condition and sustains a solid liquid interface at 9 between the-molten polycrystalline material 8 and the solid seed 5.
The solid-liquid interface at 9 is maintained in a slightly convex configuration in the direction of the molten material. This solid-liquid interface configuration results from the relatively higher horizontal heat flow with respect to the radial heat flow through the longitudinal heat conducting member 6 and illustrated by the arrows ll) in FIG. 4. Where the relative amount of heat flow in the vicinity of the liquid-solid interface is radial, the interface configuration is concave toward the molten charge and detrimental to the growth of crystals with a high degree of perfection.
The single crystal growth apparatus of this invention is further described in connection with its application to the well known process for making doped or undoped gallium arsenide and known as the Horizontal Bridgman technique.
Broadly, stoichiometric quantities of gallium and arsenic are reacted in a closedtube which is subjected to a temperature gradient of approximately 614 to 1,240C. Arsenic vaporized at the said 614C temperature and a gallium arsenide solid-liquid crystallization interface exists at about 1,240C.
A double furnace apparatus as shown in FIG. 2 is provided having a cold zone 12 and a hot zone 13 and separated by an insulating partition 14. A stoichiometric amount of polycrystalline gallium is placed in the liquid melt section 1 of the apparatus with a given amount of the desired dopant. A previously prepared seed of the desired crystallographic orientation is inserted into the seed cavity.
The apparatus containing the aforesaid materials is placed in a tube with a sufficient amount of arsenic to maintain the stoichiometry of the melt plus an excess to maintain a condensed phase at one atmosphere of pressure at about 614C.
A seal off plug is inserted into the tube and the tube evacuated to 10" Torr, whereupon the tube is conventionally sealed off by collapsing the tube onto the plug.
The tube is now inserted into the furnace and brought to thermal equilibrium and positioned so that the gallium and dopant material are located in the hot section of the furnace and maintained in a molten state. The liquid solid interface between the molten polycrystalline gallium and the seed crystal is located at a temperature of about 1,240C in the thermal gradient.
The tube is then moved at the desired crystal growth rate and with respect to the furnace from the hot zone toward the colder zone while maintaining the solidliquid interface between the molten gallium arsenide and the seed crystal within the said 1,240C temperature zone. This results in a horizontal directional freezing or crystallization of the charge. Upon completion of the crystallization of the molten charge, the tube is allowed to slowly cool to room temperature, whereby thermal shock is avoided, whereupon the tube is broken open and the apparatus containing the gallium arsenide ingot is removed.
The ingot or boule thus formed is preserved for further processing.
The use of previously known crystal growing apparatus to produce gallium arsenideingots produced acceptable product less than 10 percent of the time, while the utilization of the apparatus of this invention produced product yields greater than percent. Similarly, the reproducibility of the desired crystal orientation with respect to its longitudinal axis was greatly enhanced and improved by this apparatus. Likewise, this apparatus allows the constantreproducibility of slice geometry which is necessary and required for production type fixtures and manufacturing efficiency.
It should be clearly understood that although an apparatus having a semi-cylindrical shape is specifically illustrated, the invention herein described is not limited thereto.
While the invention has been particularly shown and described with reference to preferred embodiments thereof, it will be understood by those skilled in the art that the foregoing and other changes in form and detail may be made therein without departing from the spirit and scope of the invention.
What is claimed is:
1. An apparatus for growing monocrystalline semiconductor material comprising a primary concave-boat section adapted to contain a melt and an integral concave end section having a decreased depth and width relative to said concave primary boat section and adapted to hold a seed crystal contacting said melt, the primary and end sections disposed axially, said end section having a disc shaped radiant heat reflecting means angularly and annularly disposed to the boat axis and a heat dissipating means secured in the distal portion of said end section and extending externally thereof and forming an end section closure.
2. An apparatus in accordance with claim 1 wherein said apparatus is constructed of fused silica.
3. An apparatus in accordance with claim 1 wherein the apparatus is constructed of fused silica and having roughened surfaces except said radiant heat dissipating member.

Claims (2)

  1. 2. An apparatus in accordance with claim 1 wherein said apparatus is construCted of fused silica.
  2. 3. An apparatus in accordance with claim 1 wherein the apparatus is constructed of fused silica and having roughened surfaces except said radiant heat dissipating member.
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US3944393A (en) * 1973-11-21 1976-03-16 Monsanto Company Apparatus for horizontal production of single crystal structure
US4169755A (en) * 1977-03-16 1979-10-02 U.S. Philips Corporation Growth of crystalline rods of gallium arsenide in a crucible of specially treated fibrous silicon dioxide
US4268483A (en) * 1976-03-17 1981-05-19 Metals Research Limited Improvements in and relating to the growth of crystalline material
US4572763A (en) * 1982-07-14 1986-02-25 Zaidan Hojin Handotai Kenkyu Shinkokai Method and apparatus for performing epitaxial growth of ZnSe crystal from a melt thereof
US4764350A (en) * 1986-10-08 1988-08-16 The United States Of America As Represented By The Secretary Of The Air Force Method and apparatus for synthesizing a single crystal of indium phosphide
US5248377A (en) * 1989-12-01 1993-09-28 Grumman Aerospace Corporation Crystal-growth furnace for interface curvature control
CN105297130A (en) * 2014-06-03 2016-02-03 长春理工大学 Method and device for orientated growth of fluoride crystals by bridgman method
CN108546986A (en) * 2018-04-19 2018-09-18 中国科学院半导体研究所 Seed crystal protective device and method for monocrystal growth

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JPS5276926U (en) * 1975-12-08 1977-06-08
JPS5722150U (en) * 1980-07-15 1982-02-04
JPS5722149U (en) * 1980-07-15 1982-02-04
JPS6090890A (en) * 1983-10-24 1985-05-22 Mitsubishi Monsanto Chem Co Method for growing single crystal of inorganic compound and boat for growing single crystal
FR2614322B1 (en) * 1987-04-27 1989-07-28 Europ Propulsion GRADIENT OVEN FOR ORIENTED SOLIDIFICATION, IN PARTICULAR BY THE BRIDGMANN METHOD.

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US3198606A (en) * 1961-01-23 1965-08-03 Ibm Apparatus for growing crystals
US3240568A (en) * 1961-12-20 1966-03-15 Monsanto Co Process and apparatus for the production of single crystal compounds
US3401022A (en) * 1964-03-26 1968-09-10 Motorola Inc Apparatus for horizontal zone refining of semiconductive materials
US3453352A (en) * 1964-12-14 1969-07-01 Texas Instruments Inc Method and apparatus for producing crystalline semiconductor ribbon
US3464812A (en) * 1966-03-29 1969-09-02 Massachusetts Inst Technology Process for making solids and products thereof
US3520810A (en) * 1968-01-15 1970-07-21 Ibm Manufacture of single crystal semiconductors
US3617223A (en) * 1968-05-21 1971-11-02 Texas Instruments Inc Apparatus for forming monocrystalline ribbons of silicon
US3607054A (en) * 1969-05-05 1971-09-21 Us Army Method for extending the growth of vapor-liquid-solid grown crystals

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3944393A (en) * 1973-11-21 1976-03-16 Monsanto Company Apparatus for horizontal production of single crystal structure
US4268483A (en) * 1976-03-17 1981-05-19 Metals Research Limited Improvements in and relating to the growth of crystalline material
US4169755A (en) * 1977-03-16 1979-10-02 U.S. Philips Corporation Growth of crystalline rods of gallium arsenide in a crucible of specially treated fibrous silicon dioxide
US4572763A (en) * 1982-07-14 1986-02-25 Zaidan Hojin Handotai Kenkyu Shinkokai Method and apparatus for performing epitaxial growth of ZnSe crystal from a melt thereof
US4968491A (en) * 1982-07-14 1990-11-06 Zaidan Hojin Handotai Kenkyu Shinkokai Apparatus for performing epitaxial growth of ZNSE crystal from melt thereof
US4764350A (en) * 1986-10-08 1988-08-16 The United States Of America As Represented By The Secretary Of The Air Force Method and apparatus for synthesizing a single crystal of indium phosphide
US5248377A (en) * 1989-12-01 1993-09-28 Grumman Aerospace Corporation Crystal-growth furnace for interface curvature control
CN105297130A (en) * 2014-06-03 2016-02-03 长春理工大学 Method and device for orientated growth of fluoride crystals by bridgman method
CN108546986A (en) * 2018-04-19 2018-09-18 中国科学院半导体研究所 Seed crystal protective device and method for monocrystal growth
CN108546986B (en) * 2018-04-19 2020-09-15 中国科学院半导体研究所 Seed crystal protection device and single crystal growth method

Also Published As

Publication number Publication date
JPS4840374A (en) 1973-06-13
GB1343384A (en) 1974-01-10
DE2241710C3 (en) 1980-10-23
FR2154458B1 (en) 1978-08-04
DE2241710A1 (en) 1973-03-22
DE2241710B2 (en) 1980-03-06
JPS5239389B2 (en) 1977-10-05
FR2154458A1 (en) 1973-05-11

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