[go: up one dir, main page]

US3597171A - Method of crystallization using solvent removal by reaction - Google Patents

Method of crystallization using solvent removal by reaction Download PDF

Info

Publication number
US3597171A
US3597171A US676511A US3597171DA US3597171A US 3597171 A US3597171 A US 3597171A US 676511 A US676511 A US 676511A US 3597171D A US3597171D A US 3597171DA US 3597171 A US3597171 A US 3597171A
Authority
US
United States
Prior art keywords
solvent
solution
seed crystal
semiconductor material
silicon
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US676511A
Inventor
Wilhelmus Francisc Knippenberg
Gerrit Verspui
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
US Philips Corp
Original Assignee
US Philips Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by US Philips Corp filed Critical US Philips Corp
Application granted granted Critical
Publication of US3597171A publication Critical patent/US3597171A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • C30B17/00Single-crystal growth onto a seed which remains in the melt during growth, e.g. Nacken-Kyropoulos method
    • 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
    • C30B9/00Single-crystal growth from melt solutions using molten solvents

Definitions

  • This invention relates to the manufacture of crystals intended more particularly for semiconductor devices.
  • semiconductor crystals may be obtained by bringing a seed crystal into contact with a melt of the semiconductor material and maintaining a temperature gradient in the junction layer so that the seed crystal grows.
  • this method can be used only with materials, such as silicon and germanium, which can be melted at acceptable temperatures.
  • silicon carbide can grow on a seed crystal from a molten saturated solution in chromium at an acceptable temperature.
  • This substance is usable as a solvent, since the silicon carbide is satisfactorily soluble in it and this solvent is not absorbed by the crystal to a troublesome extent.
  • This method has been carried out at atmospheric pressure in an inert gas at a temperature slightly above the melting point of the solution, namely approximately 1800 C. As a result of the small temperature difference between the seed crystal and the solution the growing rate of the crystal was low to a troublesome extent.
  • the solvent must then have not only an acceptable solubility of the semiconductor material and not be absorbed by the crystal to a troublesome extent, but also have so high a vapour pressure at the melting temperature that sufiiciently rapid evaporation of the solvent and a rapid crystal growth, as the case may be at reduced pressure, take place.
  • An object of the invention is to mitigate this disadvantage.
  • the present invention underlies recognition of the fact that the state of oversaturation can be obtained in a simple manner by chemical means instead of by physical removal of solvent by evapoartion, possibly at reduced pressure.
  • the invention relates to a method of manufacturing crystals, e.g. crystals for semiconductor devices, in which a seed crystal is brought into contact with a molten saturated solution of a semiconductor material so that the seed crystal grows, and it is characterized in that a gas is supplied to the atmosphere above the solution which gas reacts with the solvent at the temperature of the melt, thus forming a volatile compound so that solvent is extracted from the surface layer and a state of oversaturation is caused in this layer.
  • a gas is supplied to the atmosphere above the solution which gas reacts with the solvent at the temperature of the melt, thus forming a volatile compound so that solvent is extracted from the surface layer and a state of oversaturation is caused in this layer.
  • This method of removing solvent has a less limiting influence on the choice of the solvent or at least an influence which is limiting in another sense than in the case when the said removal is to take place by evaporation at reumbled pressure.
  • the majority of substances which can be used as solvents such as gallium with gallium phosphide, silicon with silicon carbide and tin With silicon, exhibit a low vapour pressure at their melting point.
  • Chromium which can be used as a solvent for silicon carbide, is a favourable exception in this respect.
  • many of the usable solvents at their melting temperatures readily form volatile compounds with gaseous reagents, such as oxygen, sulphur and halogen, so that solvent may rapidly be extracted from the solution.
  • EXAMPLE 1 As shown in the drawing, a seed crystal 1 of gallium phosphide is laid on the surface of a saturated solution 2 consisting of 4 mol percent of gallium phosphide in gallium, which solution is contained in a graphite vessel 3 placed in a quartz tube 4 and maintained in a molten state in argon of atmospheric pressure at a temperature of 1050 C. by means of an oven 5.
  • a chlorine flow of 50 cm. per minute is passed through the quartz tube 4, causing solvent (gallium) to be extracted from the melt while forming volatile gallium chloride, so that oversaturation occurs in the surface layer and the gallium phosphide seed crystal grows at a rate of more than 30p. per hour.
  • the method according to the invention can also be carried out in such manner that the seed crystal is fixed in position relative to the graphite crucible, the seed crystal being able to grow due to the solvent disappearing and the level of the liquid in the crucible falling correspondingly.
  • EXAMPLE 2 By means of a similar device as has been described in Example 1, a solution of 5 at. percent of silicon in tin in a quartz vessel is maintained in the molten state at 900 C.
  • a method of growing crystals for use in semiconductor devices comprising the steps of forming a molten saturated solution of a semiconductor material in a solvent,
  • the semiconductor material is selected from the group consisting of silicon, silicon carbide and gallium phosphide.
  • gaseous reagent is oxygen, sulfur or a halogen.

Landscapes

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

Abstract

A METHOD OF MANUFACTURING CRYSTALS OF SEMICONDUCTOR MATERIALS IN WHICH A SEED CRYSTAL IS BROUGHT INTO CONTACT WITH A MOLTEN SATURATED SOLUTION OF THE SEMICONDUCTOR MATERIAL SHILE A GAS IS SUPPLIED TO THE ATMOSPHERE ABOVE THE SOLUTION WHICH REACTS WITH SOLVENT AT THE TEMPERATURE OF THE MELT TO FORM A VOLATILE COMPOUND SO THAT THE SOLVENT IS EXTRACTED FROM THE SURFACE LAYER AND A STATE OF OVER-SATURATION IS CAUSED IN THIS LAYER.

Description

Aug-3, 1971 w. F. KNIPPENBERG L 3,597,171
METHOD OF CRYSTALLIZATION USING SOLVENT REMOVAL BY REACTION Filed Oct. 19, 1967 WIL HELM HiVENTORS US KNIPPEN R GERRIT VERSPUI BE 6 iawa z. AGENT United States Patent O1 3,597,171 Patented Aug. 3, 1971 ice U.S. Cl. 23-3015 6 Claims ABSTRACT OF THE DISCLOSURE A method of manufacturing crystals of semiconductor materials in which a seed crystal is brought into contact with a molten saturated solution of the semiconductor material while a gas is supplied to the atmosphere above the solution which reacts with solvent at the temperature of the melt to form a volatile compound so that the solvent is extracted from the surface layer and a state of over-saturation is caused in this layer.
This invention relates to the manufacture of crystals intended more particularly for semiconductor devices.
It is known that semiconductor crystals may be obtained by bringing a seed crystal into contact with a melt of the semiconductor material and maintaining a temperature gradient in the junction layer so that the seed crystal grows.
As a matter of fact, this method can be used only with materials, such as silicon and germanium, which can be melted at acceptable temperatures.
It is also known that silicon carbide can grow on a seed crystal from a molten saturated solution in chromium at an acceptable temperature. This substance is usable as a solvent, since the silicon carbide is satisfactorily soluble in it and this solvent is not absorbed by the crystal to a troublesome extent. This method has been carried out at atmospheric pressure in an inert gas at a temperature slightly above the melting point of the solution, namely approximately 1800 C. As a result of the small temperature difference between the seed crystal and the solution the growing rate of the crystal was low to a troublesome extent.
This may be considerably improved by crystallising at a reduced gas pressure whereby the solvent evaporates. A state of oversaturation is then caused in the surface layer with which the seed crystal is in contact, resulting in a crystal growth which is sped up considerably.
It is also known that such a method is also interesting for semiconductor materials other than silicon carbides. This holds good not only for semiconductor compounds, such as gallium phosphide, which cannot be crystallised directly from a melt or with great difiiculty only, but also for semiconductor elementary materials, such as silicon, which when dissolved in a low-melting temperature solvent, for example tin, can be crystallised at comparatively low temperatures.
However, as previously mentioned, the solvent must then have not only an acceptable solubility of the semiconductor material and not be absorbed by the crystal to a troublesome extent, but also have so high a vapour pressure at the melting temperature that sufiiciently rapid evaporation of the solvent and a rapid crystal growth, as the case may be at reduced pressure, take place.
The latter requirement as regards the solvent results in that the choice of a solvent for crystallising a given semiconductor is greatly limited and in certain cases a serviceable solvent will not even be available.
An object of the invention is to mitigate this disadvantage.
The present invention underlies recognition of the fact that the state of oversaturation can be obtained in a simple manner by chemical means instead of by physical removal of solvent by evapoartion, possibly at reduced pressure.
The invention relates to a method of manufacturing crystals, e.g. crystals for semiconductor devices, in which a seed crystal is brought into contact with a molten saturated solution of a semiconductor material so that the seed crystal grows, and it is characterized in that a gas is supplied to the atmosphere above the solution which gas reacts with the solvent at the temperature of the melt, thus forming a volatile compound so that solvent is extracted from the surface layer and a state of oversaturation is caused in this layer.
This method of removing solvent has a less limiting influence on the choice of the solvent or at least an influence which is limiting in another sense than in the case when the said removal is to take place by evaporation at re duced pressure. In fact, the majority of substances which can be used as solvents, such as gallium with gallium phosphide, silicon with silicon carbide and tin With silicon, exhibit a low vapour pressure at their melting point. Chromium, which can be used as a solvent for silicon carbide, is a favourable exception in this respect. However, many of the usable solvents at their melting temperatures readily form volatile compounds with gaseous reagents, such as oxygen, sulphur and halogen, so that solvent may rapidly be extracted from the solution.
EXAMPLE 1 As shown in the drawing, a seed crystal 1 of gallium phosphide is laid on the surface of a saturated solution 2 consisting of 4 mol percent of gallium phosphide in gallium, which solution is contained in a graphite vessel 3 placed in a quartz tube 4 and maintained in a molten state in argon of atmospheric pressure at a temperature of 1050 C. by means of an oven 5.
Subsequently a chlorine flow of 50 cm. per minute is passed through the quartz tube 4, causing solvent (gallium) to be extracted from the melt while forming volatile gallium chloride, so that oversaturation occurs in the surface layer and the gallium phosphide seed crystal grows at a rate of more than 30p. per hour.
In conclusion, it should be noted that the method according to the invention can also be carried out in such manner that the seed crystal is fixed in position relative to the graphite crucible, the seed crystal being able to grow due to the solvent disappearing and the level of the liquid in the crucible falling correspondingly.
EXAMPLE 2 By means of a similar device as has been described in Example 1, a solution of 5 at. percent of silicon in tin in a quartz vessel is maintained in the molten state at 900 C.
On passing through the vessel hydrochloric acid gas of atmospheric pressure at a rate of cm. per minute a silicon seed crystal laid on the solution grows at a rate of 25,11. per hour. This growth takes place due to the oversaturation in the surface layer which is caused by the extraction of solvent (tin) in the form of volatile tin chloride from the solution.
If solvent is extracted from the solution by evaporation in an argon atmosphere at a pressure of 10 mms., a crystal growth of only 10 per hour is obtained at the same temperature.
What is claimed is:
1. A method of growing crystals for use in semiconductor devices comprising the steps of forming a molten saturated solution of a semiconductor material in a solvent,
bringing into contact with a surface layer of the molten solution a seed crystal of said semiconductor material, and supplying to the atmosphere above the molten solution a gaseous reagent which reacts with the solvent at the melt temperature to form a volatile compound which vaporizes from said surface layer removing solvent from said molten solution and super-saturating said molten solution whereby semiconductor material is precipitated onto the seed crystal causing growth thereof.
2. A method as claimed in claim 1, wherein the semiconductor material is selected from the group consisting of silicon, silicon carbide and gallium phosphide.
3. A method as claimed in claim 2 wherein the semiconductor material is gallium phosphide and the solvent is gallium.
4. A method as claimed in claim 2 wherein the semiconductor material is silicon and the solvent is tin.
5. A method as claimed in claim 2 wherein the semiconductor material is silicon carbide and the solvent is silicon or chromium.
6. A method as claimed in claim 2 wherein the gaseous reagent is oxygen, sulfur or a halogen.
References Cited NORMAN YUDKOFF, Primary Examiner R. T. FOSTER, Assistant Examiner US. Cl. X.R.
US676511A 1966-10-22 1967-10-19 Method of crystallization using solvent removal by reaction Expired - Lifetime US3597171A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL6614999A NL6614999A (en) 1966-10-22 1966-10-22

Publications (1)

Publication Number Publication Date
US3597171A true US3597171A (en) 1971-08-03

Family

ID=19797982

Family Applications (1)

Application Number Title Priority Date Filing Date
US676511A Expired - Lifetime US3597171A (en) 1966-10-22 1967-10-19 Method of crystallization using solvent removal by reaction

Country Status (9)

Country Link
US (1) US3597171A (en)
AT (1) AT270754B (en)
BE (1) BE705462A (en)
CH (1) CH494065A (en)
DE (1) DE1619987B2 (en)
DK (1) DK115390B (en)
GB (1) GB1165037A (en)
NL (1) NL6614999A (en)
SE (1) SE309966B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3996891A (en) * 1974-03-01 1976-12-14 Sony Corporation Liquid phase epitaxial growth apparatus wherein contacted wafer floats
US4415545A (en) * 1980-12-15 1983-11-15 Monkowski Joseph R Solid film growth via preferential etching of liquid solutions
US5544616A (en) * 1992-05-13 1996-08-13 Midwest Research Institute Crystallization from high temperature solutions of Si in Cu/Al solvent

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3996891A (en) * 1974-03-01 1976-12-14 Sony Corporation Liquid phase epitaxial growth apparatus wherein contacted wafer floats
US4415545A (en) * 1980-12-15 1983-11-15 Monkowski Joseph R Solid film growth via preferential etching of liquid solutions
US5544616A (en) * 1992-05-13 1996-08-13 Midwest Research Institute Crystallization from high temperature solutions of Si in Cu/Al solvent

Also Published As

Publication number Publication date
DK115390B (en) 1969-10-06
BE705462A (en) 1968-04-22
GB1165037A (en) 1969-09-24
SE309966B (en) 1969-04-14
DE1619987B2 (en) 1977-01-20
DE1619987A1 (en) 1970-03-26
CH494065A (en) 1970-07-31
AT270754B (en) 1969-05-12
NL6614999A (en) 1968-04-23

Similar Documents

Publication Publication Date Title
Kaiser et al. Nitrogen in silicon
JP2001106600A (en) Method for growing silicon carbide crystal in liquid phase
Harman Slider LPE of Hg1-xCdxTe using mercury pressure controlled growth solutions
US3597171A (en) Method of crystallization using solvent removal by reaction
JP4934958B2 (en) Method for producing silicon carbide single crystal
US3353914A (en) Method of seed-pulling beta silicon carbide crystals from a melt containing silver and the product thereof
BRPI0609475A2 (en) process to convert sici4 to itself metallic
US5211801A (en) Method for manufacturing single-crystal silicon carbide
US3649193A (en) Method of forming and regularly growing a semiconductor compound
JPS61178495A (en) Method for growing single crystal
Wagner A solid-liquid-vapor etching process
CA1319588C (en) Method of making single-crystal mercury cadmium telluride layers
Wardill et al. The preparation and assessment of indium phosphide
US3519399A (en) Method for growing single crystals of semiconductors
US3816601A (en) Process for the production of pure metal halides
Tonn et al. Removal of oxidic impurities for the growth of high purity lead iodide single crystals
SU339134A1 (en) Method of building-up diamond facets
US3694166A (en) Crystal growth tube
US3374067A (en) Process of growing cubic zinc sulfide crystals in a molten salt solvent
JPH0585893A (en) Process for producing semiconductor foil and its usage
US4415545A (en) Solid film growth via preferential etching of liquid solutions
JPS63250428A (en) Method for purifying indium
US3607054A (en) Method for extending the growth of vapor-liquid-solid grown crystals
US3635753A (en) Growth of needlelike vls crystals
Sashital Growth of single crystal layers of AgGaS2 by liquid phase epitaxy using halide fluxes