US3922467A - Vapour-phase deposition method - Google Patents

Vapour-phase deposition method Download PDF

Info

Publication number
US3922467A
US3922467A US464574A US46457474A US3922467A US 3922467 A US3922467 A US 3922467A US 464574 A US464574 A US 464574A US 46457474 A US46457474 A US 46457474A US 3922467 A US3922467 A US 3922467A
Authority
US
United States
Prior art keywords
substrates
substrate
gas flow
gas
space
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
US464574A
Inventor
Pierre Pinchon
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 US3922467A publication Critical patent/US3922467A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/458Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for supporting substrates in the reaction chamber
    • C23C16/4582Rigid and flat substrates, e.g. plates or discs
    • C23C16/4587Rigid and flat substrates, e.g. plates or discs the substrate being supported substantially vertically
    • 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
    • Y10S148/00Metal treatment
    • Y10S148/006Apparatus
    • 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
    • Y10S148/00Metal treatment
    • Y10S148/065Gp III-V generic compounds-processing

Definitions

  • the present invention relates to a method of forming a deposit on a large number of flat substrates at a given temperature, according to which method the said substrates are provided in a zone of a tubular space, after which a gas mixture which contains the elements to be deposited and the temperature of which is higher than that of the said zone is conveyed into the said space in the direction of the substrates.
  • a shift of the equilibrium of a chemical reaction is usually employed: a gas mixture which is chemically stable at a temperature T, is passed over the substrate at a temperature T which is lower than T
  • the reaction which the deposition causes upon contact of the substrate is very slow.
  • the consumption of reacting elements is not negligible and is in particular much larger than during a diffusion operation, for example, that of a doping element in a semiconductor substrate in which the quantity of material actually diffused in the substrate is comparatively small.
  • the latter When for series production the deposition operation is simultaneously carried out on the largest possible number of substrates, the latter should be provided in the same space and a gas flow with the elements should be conveyed over each of the substrates. If the substrates are provided parallel to the gas flow and are reached successively by the latter which flows laminarly over the receiving surfaces, the gas mixture gradually depletes in reaction elements and the thickness of the deposit decreases from the substrate which is nearest to the inlet of the reaction gas to the substrate which is farthest remote. It has been endeavoured to correct the effect of said depletion. by means of a temperature gradient along the track of the gas flow. However, the possibilities of correction are restricted by the kinetics of the reaction, the gradient is difficult to maintain and involves a variation of the composition of the deposit and/or of a possible concentration of doping impurities when a doped semiconductor in concerned.
  • the substrates have been provided in the form of a corn ear, either at right angles to the gas flow, or with a certain inclination in one direction or in the other, the drawback of the depletion of the gas 'flow of reaction elements has not been removed even in the case in which the support which is used for holding the substrates is in the form of a grating as is described, for example, in the US. Pat. No. 3,678,893, according to which the receiving surface of the substrates is directed downwards and opposite to the inlet of the gas flow; the substrates placed near the inlet of the reaction gas see their deposit grow more rapidly than that of the substrates which are farther remote from said inlet.
  • Another object of the invention is the compensation of the depletion of reaction elements of a gas flow which is used on a series of substrates placed along said flow, so as to obtain the same effect on saiddifferent substrates.
  • Another object of the invention is to obtain an epitaxial deposit of a thickness between certain tolerance limits on an assembly of crystalline substrates starting from elements in the gaseous phase.
  • the method of forming a deposit on a large number of flat substrates at a given temperature is characterized in that the said substrates are placed in such manner in places along the track of the gas mixture in the said space that the successive distances between adjacent substrates increase from the first substrate which is reached by the gas flow to the substrate which is nearest to the point of removal of the said flow.
  • the substrates are present laterally relative to the gas flow which forms the mixture in the tubular space and are not reached directly by said mixture; by diffusion from the said gas flow, the components of the mixture with the elements to be deposited can reach the receiving surfaces.
  • the velocity of said diffusion is a function of various factors which depend on the gas flow itself and also on the intermediate space between the substrates. Applicants have found that the reaction rate and consequently the rate of deposition on a substrate was more rapid according as the intermediate space between said substrate and the adjacent substrate was larger.
  • the gas mixture which supplies the elements to be deposited diffuses in the spaces between the substrates and depletes along the track thereof in the space due to the consumption of elements forming the deposit: the increase of the intermediate space between the substrates varies the diffusion circumstances and has for its object to compensate for the consequences of said depletion.
  • the rates of deposition of the various substrates reach an equilibrium,-the resulting thicknesses of deposition are substantially the same after a certain time.
  • the substrates generally consist of small plates which usually are rectangular or circular. Said substrates may have a small diameter or a less regular shape or dimensions differing from each other. Irrespective of the dimensions and the shape of the substrates, the diffusion effect of the gas flow is preferably ensured by securing each of the substrates on a support which is flat and thin and the surface of which exceeds that of the substrate and which is manufactured from a material on which the deposit cannot be effected chemically. Said supports mutually determine a succession of diffusion volumes in which the substrates are placed. The diffusion effect and the influence of the mutual distance between the substrates or the supports are thus used in the best of circumstances.
  • the danger is to be avoided of obtaining a difference in thickness, in deposition quality, between the substrates whose surface would be directed in the direction of flow of the gas mixture and of the substrates whose surface would be directed in the opposite direction.
  • This danger is avoided by directing all the substrates in the same direction and by securing the substrates only to one face of each support when supports are used.
  • the substrates are provided, for example, in such manner that their receiving surface is present opposite to the supply direction of the gas flow in the space. In this case no substrate is placed on the first support present opposite to 3 the inlet of the gas mixture: this support serves as a screen.
  • the tubular space in which the substrates are provided and into which the gas mixture is conveyed has a substantially rectangular cross-section and the substrate supports are also rectangular and placed in such manner that two symmetrical gas flows are formed of substantially identical rectangular cross-section; the diffusion occurs from said flow in two concurrent directions, which reduces the possible differences in deposition thickness on the same substrate.
  • the'tubular space in which the substrates are placed and into which the gas mixture is conveyed has a circular cross-section and the substrates and supports are placed in the axis of the space.
  • the means which determine the position of the supports relative to the space are provided with the object of disturbing the gas flow in a minimum possible manner from which the diffusion to the substrates should occur nearly uniformly in order to minimize the differences in deposition thickness which may occur in one or another point of the substrate, in particular when said substrate has a comparatively large area.
  • the space used for carrying out the method according to the invention can be directed in any manner.
  • the law of the enlargement of the intermediate space which is to enable the compensation of depletion of the gas mixture in elements which are necessary to form a deposit is determined experimentally; indeed the depletion along the gas flow is a function of numerous factors which depend especially on the deposited bodies, on the composition of the gas mixture, on the shape and on the dimensions of the space and on the temperatures of the gas mixture and the substrates.
  • the enlargement of the intermediate spaces preferably is substantially linear. For example, in the case of supports the largest dimension of which is 20 to 80 mm, the minimum intermediate space is 5 to mm and the enlargement is 0.5 to 2 mm per intermediate space.
  • the doping concentration can be kept constant for each individual substrate by simultaneously producing an enlargement of the intermediate spaces between substrates and a temperature gradient of one substrate to the other, while a single temperature gradient, even when this enables the partial compensation of the gradual depletion effect of the gas flow on the thickness of deposition, involves an undesired variation of the doping.
  • the invention may be used for depositing material which can be formed in the vapour phase by reaction of compounds the equilibrium of which is varied by reducing the temperature.
  • the invention is used in particular for depositing semiconductor materials, polycrystalline or monocrystalline materials.
  • the method according to the invention may be used in particular for the epitaxial monocrystalline deposition of semiconductor compounds which comprise at least one element of the columns II and III of the Periodic Table of elements and at least one element of the columns V and VI of said Table, for example, gallium arsenide phosphide which is deposited from gallium chloride and gaseous compounds of phosphorus and arsenic in a hydrogen flow. In that case, for example, silicon or oxidized silicon is used.
  • the present invention also relates to plates of crystalline semiconductor material with an epitaxial deposit which has been realized according to the method in the various embodiments described.
  • FIG. 1 is a diagrammatic longitudinal cross-sectional view of a deposition device according to a known method with graphs indicating the temperatures used and the resulting thicknesses.
  • FIG. 2 is a diagrammatic longitudinal cross-sectional view showing an arrangement of substrates according to the invention. 7
  • FIG. 3 is a diagrammatic longitudinal cross-sectional view of a device for depositing according to the invention.
  • FIG. 4 is a cross-sectional view taken on the line BB of FIG. 5 of a device for depositing according to the invention.
  • FIG. 5 is a longitudinal cross-sectional view taken on the line AA of FIG. 4 of the same device.
  • said substrates may be placed on a rack 2 which is placed in a tubular space.
  • a gas mixture which chemically is in equilibrium at a temperature T is conveyed at 4, the substrates 3 being maintained at a temperature T, which is lower than T,.
  • the gas flow 5 depletes due to the consumption of deposited elements, and the gas mixture removed at 6 has a weaker concentration than in the supply thereof at 4 (the content of non-used side products of the reaction may be higher on the contrary).
  • the substrates 3 are present at the same mutual distance either because they are arranged at right angles to the gas flow as shown in FIG.
  • the thickness of the deposit obtained on the substrate is not regular because the substrates reached first receive a thicker deposit than the substrates reached last.
  • the difference in thickness between the first substrate 3a and the last 32 is considerable.
  • the curve C which is drawn with respect to the diagrammatic cross-section of the space shows the variation of the thickness obtained as a function of the distance X which separates one of the substrates from the substrate 3a.
  • a temperature gradient may be produced along the space 1; the curve of the temperature T as a function of the distance X, which is C in the case of a temperature which is equal for all the substrates, may then be replaced by the curve C.
  • deposition thicknesses are obtained according to the curve C, which are spread from c to e e
  • he substrates are placed, for example, in the manner as shown in FIG. 2.
  • Substrates 23 are secured to flat and thin supporting plates 22 perpendicularly to the gas flow indicated by the arrow 24 which flows in the longitudinal direction in a space 21 and diffuses towards the substrates 23 according to the directions denoted by the arrows 25.
  • the supports are placed in the space in such manner that a space is formed around it which forms a tube for passing the reaction gas mixture, the distances between each substrate and the adjacent support increasing in the direction of flow of the gas flow 24; if the distance is equal to d for the substrate of the n" order and ti for the substrate of the (n+1)" order, one has d d,,.
  • the minimum mutual distance d between the first substrate and the following support is determined as a function of the tolerance which is permitted for the uniformity of the thickness of the deposit on each substrate.
  • the receiving surfaces of the substrates shown in FIG. 2 are not present opposite to the inlet of the gas flow but in the opposite direction.
  • the substrates 33 shown in FIG. 3 on the contrary are secured to supports 32 in a tubular space 31 and are present opposite to the supply direction of the vapour mixture which forms the gas flow 34.
  • the distance d between each substrate and the adjacent support increases in the direction of the gas flow.
  • a plate 36 which is identical to the support 32 is placed in front of said substrate 35.
  • Rectangular substrates 43 bear ton rectangular very slightly inclined supports 42 which form part of a plate 47. Said supports are secured, for example, on the platform by means of angle pieces 49 of minimum dimensions in such manner that the diffusion in the space 40 between the supports and the substrates is not disturbed. The latter are held in place by gravity and due to the abument studs 48.
  • the platform 47 is placed in a tubular reactor 41 of a rectangular cross-section in such manner that two similar passages 44 and 45 remain on either side of the supports for the flow of the gas which enters at 51 and then diffuses in the spaces 40 the width of which gradually increases. The diffusion from the two gas flows occurs symmetrically.
  • a plate 46 which is identical to the supports 42 avoids that the first substrate is directly exposed to the gas flow which enters the space.
  • a platform having 20 supports of oxidized silicon 19 supports of gallium arsenide are provided.
  • the dimensions of the supports are 40 X 40 mm and the mutual intermediate space d between the adjacent supports varies from 10 to 20 mm according to a substantially linear arithmetical series.
  • the platform with its charge is placed in a tubular reactor having inside cross-sections of X 40 mm, two passages of 40 X 15 mm being left free for the flow of the gas mixture on either side of the supports.
  • the platform is directed so that the first support which does not support a substrate is present on the side of the gas supply which is also that of the minimum mutual intermediate space d.
  • the reactor is purified by means of hydrogen and then heated to the desired temperature, from which instant the substrates are maintained at a temperature between 750 and 800C with a gradient of 10 between the various substrate ends.
  • a gas mixture containing the elements which are to be deposited, including the possible doping elements, and diluted with hydrogen and heated to a temperature of approximately 900C' is conveyed to the platform with substrates with a total supply in the order to 10 liters per minute.
  • a deposit of gallium arsenide phosphide carried out in these conditions and having an average thickness of 60 micrometers shows a maximum difference of 5% between the thicknesses deposited on the various substrates, as well as a difference of less than 20% between the concentrations of doping impurities.
  • a method of forming a deposit on a large number of flat substrates by reaction of a gaseous mixture of compounds of the elements to be deposited comprising passing a gas flow containing gaseous compounds of the elements to be deposited through the zone of a tubular space containing the substrates arranged with their flat surfaces substantially perpendicular to the direction of the gas flow and each substrate being separated from the next substrate by a distance that increases in the direction of the flow of the gas, said gas being heated to a temperature above that of said substrates and depositing said elements on said substrates.
  • each substrate is secured on a thin and flat support which has an area which is larger than that of the substrate secured thereto.
  • each support supports only one substrate on one surface, all the substrates with their receiving surface being directed in the same direction as the gas flow.

Abstract

A method of forming a deposit from a gas mixture on a large number of flat substrates in a tubular space. The substrates are arranged along the gas flow with increasing spaces between substrates from the substrate reached first by the mixture to the substrate reached last by the mixture. Application to the epitaxial deposition of semiconductor compounds.

Description

United States Patent Pinchon Nov. 25, 1975 [54] VAPOUR-PHASE DEPOSITION METHOD 3,678,893 7/1972 Bell 118/500 Inventor Pierre Pinchon Caen France 3,816,166 6/1974 Eversteijn et al. 117/106 A [73] Assignee: U.S. Philips Corporation, New
York, N.Y. Primary ExaminerHarris A. Pitlick Attorney, Agent, or Firm-Frank R. Trifari; Norman [22] Flled. Apr. 26, 1974 N Spain [21] Appl. No.: 464,574
[30] Foreign Application Priority Data [57] ABSTRACT Apr. 27, 1973 France 73.15461 A method of forming a deposit from a gas mixture on [52'] a large number of flat substrates in a tubular space.
' 427/24;427/252;427/25 The substrates are arranged along the gas flow with 51 1m.c1. c23c 11/00 increasing Spaces between Substrates from the [58] Field of searchmn 117/106 R 106 A 1072 R substrate reached first by the mixture to the substrate 117/201; 118/48, 49, 49.1, 49.5, 500 reached last by Application to the epitaxial deposition of [56] References Cited semiconductor compounds.
UNITED STATES PATENTS 3,409,483 11/1968 Watson 148/175 6 Claims, 5 Drawing Figures 31; 3 3 )31 34 1 "n," "mum 4 m, ,5,
IIIIIIII/IIIIlI/lI/IlIl/l,
Sheet 1 of 2 US. Patent Nov. 25, 1975 I 32 nun? r 44" Egnunnn US. Ht NOV. 25, Sheet 2 f 3 7 VAPOUR-PHASE DEPOSITION METHOD The present invention relates to a method of forming a deposit on a large number of flat substrates at a given temperature, according to which method the said substrates are provided in a zone of a tubular space, after which a gas mixture which contains the elements to be deposited and the temperature of which is higher than that of the said zone is conveyed into the said space in the direction of the substrates.
For depositing an epitaxial layer, for example, of semi-conductor material, on a suitable substrate from elements in the vapour phase, a shift of the equilibrium of a chemical reaction is usually employed: a gas mixture which is chemically stable at a temperature T, is passed over the substrate at a temperature T which is lower than T The reaction which the deposition causes upon contact of the substrate is very slow. Taking into account the small gas flow, the consumption of reacting elements is not negligible and is in particular much larger than during a diffusion operation, for example, that of a doping element in a semiconductor substrate in which the quantity of material actually diffused in the substrate is comparatively small.
When for series production the deposition operation is simultaneously carried out on the largest possible number of substrates, the latter should be provided in the same space and a gas flow with the elements should be conveyed over each of the substrates. If the substrates are provided parallel to the gas flow and are reached successively by the latter which flows laminarly over the receiving surfaces, the gas mixture gradually depletes in reaction elements and the thickness of the deposit decreases from the substrate which is nearest to the inlet of the reaction gas to the substrate which is farthest remote. It has been endeavoured to correct the effect of said depletion. by means of a temperature gradient along the track of the gas flow. However, the possibilities of correction are restricted by the kinetics of the reaction, the gradient is difficult to maintain and involves a variation of the composition of the deposit and/or of a possible concentration of doping impurities when a doped semiconductor in concerned.
If the substrates have been provided in the form of a corn ear, either at right angles to the gas flow, or with a certain inclination in one direction or in the other, the drawback of the depletion of the gas 'flow of reaction elements has not been removed even in the case in which the support which is used for holding the substrates is in the form of a grating as is described, for example, in the US. Pat. No. 3,678,893, according to which the receiving surface of the substrates is directed downwards and opposite to the inlet of the gas flow; the substrates placed near the inlet of the reaction gas see their deposit grow more rapidly than that of the substrates which are farther remote from said inlet.
It is the object of the present invention to mitigate this drawback of the known method and to make it possible to obtain deposits of substantially the same thickness and quality on a larger number of substrates.
Another object of the invention is the compensation of the depletion of reaction elements of a gas flow which is used on a series of substrates placed along said flow, so as to obtain the same effect on saiddifferent substrates.
Another object of the invention is to obtain an epitaxial deposit of a thickness between certain tolerance limits on an assembly of crystalline substrates starting from elements in the gaseous phase.
According to the invention, the method of forming a deposit on a large number of flat substrates at a given temperature, according to which method the said substrates are provided in a zone of a tubular space, after which a gas mixture containing the elements which serve to be deposited and the temperature of which is higher than that of the said zone is conveyed into the said space in the direction of the said substrates, is characterized in that the said substrates are placed in such manner in places along the track of the gas mixture in the said space that the successive distances between adjacent substrates increase from the first substrate which is reached by the gas flow to the substrate which is nearest to the point of removal of the said flow.
The substrates are present laterally relative to the gas flow which forms the mixture in the tubular space and are not reached directly by said mixture; by diffusion from the said gas flow, the components of the mixture with the elements to be deposited can reach the receiving surfaces. The velocity of said diffusion is a function of various factors which depend on the gas flow itself and also on the intermediate space between the substrates. Applicants have found that the reaction rate and consequently the rate of deposition on a substrate was more rapid according as the intermediate space between said substrate and the adjacent substrate was larger. The gas mixture which supplies the elements to be deposited diffuses in the spaces between the substrates and depletes along the track thereof in the space due to the consumption of elements forming the deposit: the increase of the intermediate space between the substrates varies the diffusion circumstances and has for its object to compensate for the consequences of said depletion. The rates of deposition of the various substrates reach an equilibrium,-the resulting thicknesses of deposition are substantially the same after a certain time.
The substrates generally consist of small plates which usually are rectangular or circular. Said substrates may have a small diameter or a less regular shape or dimensions differing from each other. Irrespective of the dimensions and the shape of the substrates, the diffusion effect of the gas flow is preferably ensured by securing each of the substrates on a support which is flat and thin and the surface of which exceeds that of the substrate and which is manufactured from a material on which the deposit cannot be effected chemically. Said supports mutually determine a succession of diffusion volumes in which the substrates are placed. The diffusion effect and the influence of the mutual distance between the substrates or the supports are thus used in the best of circumstances.
When the velocity of the gas flow is high, the danger is to be avoided of obtaining a difference in thickness, in deposition quality, between the substrates whose surface would be directed in the direction of flow of the gas mixture and of the substrates whose surface would be directed in the opposite direction. This danger is avoided by directing all the substrates in the same direction and by securing the substrates only to one face of each support when supports are used. The substrates are provided, for example, in such manner that their receiving surface is present opposite to the supply direction of the gas flow in the space. In this case no substrate is placed on the first support present opposite to 3 the inlet of the gas mixture: this support serves as a screen.
In a preferred embodiment of the invention the tubular space in which the substrates are provided and into which the gas mixture is conveyed has a substantially rectangular cross-section and the substrate supports are also rectangular and placed in such manner that two symmetrical gas flows are formed of substantially identical rectangular cross-section; the diffusion occurs from said flow in two concurrent directions, which reduces the possible differences in deposition thickness on the same substrate.
In another embodiment of the invention the'tubular space in which the substrates are placed and into which the gas mixture is conveyed has a circular cross-section and the substrates and supports are placed in the axis of the space.
The means which determine the position of the supports relative to the space, for example, a grating, are provided with the object of disturbing the gas flow in a minimum possible manner from which the diffusion to the substrates should occur nearly uniformly in order to minimize the differences in deposition thickness which may occur in one or another point of the substrate, in particular when said substrate has a comparatively large area.
Large quantities of substrates can be treated simultaneously in a tubular space used according to the invention. It is possible to treat several parallel rows of supports and substrates between which the flow of the gas mixture occurs in the same space having sufficient dimensions. The treatment of a large number of substrates in the same operation form a single gas supply ensures the homogeneity of the composition of the deposit which otherwise can be ensured with greater difficulty by a repetition of a treatment for each time a small number of substrates.
It is obvious that the space used for carrying out the method according to the invention can be directed in any manner. However, it is more advantageous to place said space in such manner that the receiving surface of the substrates is approximately vertical, which avoids the danger of contamination of the deposit by impurities which fall on said receiving surfaces under the influence of gravity.
The law of the enlargement of the intermediate space which is to enable the compensation of depletion of the gas mixture in elements which are necessary to form a deposit is determined experimentally; indeed the depletion along the gas flow is a function of numerous factors which depend especially on the deposited bodies, on the composition of the gas mixture, on the shape and on the dimensions of the space and on the temperatures of the gas mixture and the substrates. The enlargement of the intermediate spaces preferably is substantially linear. For example, in the case of supports the largest dimension of which is 20 to 80 mm, the minimum intermediate space is 5 to mm and the enlargement is 0.5 to 2 mm per intermediate space. Experience teaches that it is advantageous to simultaneously use the two factors determining the rate of deposition on the substrates: on the one hand the temperature of the substrates, on the other hand the intermediate spaces between the substrates. The combination of a temperature gradient along a row of substrates and of an enlargement of the intermediate spaces between the substrates makes it possible to obtain a uniformity of the deposition thicknesses, simultaneously with a homogeneity of the composition of the deposit. For example, in the case of a deposit of a semiconductor material, the doping concentration can be kept constant for each individual substrate by simultaneously producing an enlargement of the intermediate spaces between substrates and a temperature gradient of one substrate to the other, while a single temperature gradient, even when this enables the partial compensation of the gradual depletion effect of the gas flow on the thickness of deposition, involves an undesired variation of the doping.
The invention may be used for depositing material which can be formed in the vapour phase by reaction of compounds the equilibrium of which is varied by reducing the temperature. The invention is used in particular for depositing semiconductor materials, polycrystalline or monocrystalline materials. The method according to the invention may be used in particular for the epitaxial monocrystalline deposition of semiconductor compounds which comprise at least one element of the columns II and III of the Periodic Table of elements and at least one element of the columns V and VI of said Table, for example, gallium arsenide phosphide which is deposited from gallium chloride and gaseous compounds of phosphorus and arsenic in a hydrogen flow. In that case, for example, silicon or oxidized silicon is used.
The present invention also relates to plates of crystalline semiconductor material with an epitaxial deposit which has been realized according to the method in the various embodiments described.
The invention will be described in greater detail with reference to the accompanying drawing, in which FIG. 1 is a diagrammatic longitudinal cross-sectional view of a deposition device according to a known method with graphs indicating the temperatures used and the resulting thicknesses.
FIG. 2 is a diagrammatic longitudinal cross-sectional view showing an arrangement of substrates according to the invention. 7
FIG. 3 is a diagrammatic longitudinal cross-sectional view of a device for depositing according to the invention.
FIG. 4 is a cross-sectional view taken on the line BB of FIG. 5 of a device for depositing according to the invention.
FIG. 5 is a longitudinal cross-sectional view taken on the line AA of FIG. 4 of the same device.
In order to perform an epitaxial semiconductor deposit on a large number of substrates 3 (FIG. 1), according to the known methods said substrates may be placed on a rack 2 which is placed in a tubular space. A gas mixture which chemically is in equilibrium at a temperature T, is conveyed at 4, the substrates 3 being maintained at a temperature T, which is lower than T,. During the track in the space the gas flow 5 depletes due to the consumption of deposited elements, and the gas mixture removed at 6 has a weaker concentration than in the supply thereof at 4 (the content of non-used side products of the reaction may be higher on the contrary). When the substrates 3 are present at the same mutual distance either because they are arranged at right angles to the gas flow as shown in FIG. 1, or because they are arranged parallel to said flow, the thickness of the deposit obtained on the substrate is not regular because the substrates reached frist receive a thicker deposit than the substrates reached last. The difference in thickness between the first substrate 3a and the last 32 is considerable. The curve C which is drawn with respect to the diagrammatic cross-section of the space shows the variation of the thickness obtained as a function of the distance X which separates one of the substrates from the substrate 3a. In order to diminish the difference between e thickness of the deposit of the substrate 3a, and e,, thickness of the deposit on the substrate 3z, a temperature gradient may be produced along the space 1; the curve of the temperature T as a function of the distance X, which is C in the case of a temperature which is equal for all the substrates, may then be replaced by the curve C The gradual drop of the temperature of the substrates between T and T only very partly compensates for the depletion of the gas flow: deposition thicknesses are obtained according to the curve C, which are spread from c to e e In order to mitigate this drawback, according to the invention he substrates are placed, for example, in the manner as shown in FIG. 2. Substrates 23 are secured to flat and thin supporting plates 22 perpendicularly to the gas flow indicated by the arrow 24 which flows in the longitudinal direction in a space 21 and diffuses towards the substrates 23 according to the directions denoted by the arrows 25. The supports are placed in the space in such manner that a space is formed around it which forms a tube for passing the reaction gas mixture, the distances between each substrate and the adjacent support increasing in the direction of flow of the gas flow 24; if the distance is equal to d for the substrate of the n" order and ti for the substrate of the (n+1)" order, one has d d,,. The minimum mutual distance d between the first substrate and the following support is determined as a function of the tolerance which is permitted for the uniformity of the thickness of the deposit on each substrate.
The receiving surfaces of the substrates shown in FIG. 2 are not present opposite to the inlet of the gas flow but in the opposite direction. The substrates 33 shown in FIG. 3 on the contrary are secured to supports 32 in a tubular space 31 and are present opposite to the supply direction of the vapour mixture which forms the gas flow 34. The distance d between each substrate and the adjacent support increases in the direction of the gas flow. In order to avoid the direct contact of the reaction mixture with the substrate 35 reached first, a plate 36 which is identical to the support 32 is placed in front of said substrate 35.
It is a similar measure which is taken in the device ishown in FIGS. 4 and 5. Rectangular substrates 43 bear ton rectangular very slightly inclined supports 42 which form part of a plate 47. Said supports are secured, for example, on the platform by means of angle pieces 49 of minimum dimensions in such manner that the diffusion in the space 40 between the supports and the substrates is not disturbed. The latter are held in place by gravity and due to the abument studs 48. The platform 47 is placed in a tubular reactor 41 of a rectangular cross-section in such manner that two similar passages 44 and 45 remain on either side of the supports for the flow of the gas which enters at 51 and then diffuses in the spaces 40 the width of which gradually increases. The diffusion from the two gas flows occurs symmetrically.
A plate 46 which is identical to the supports 42 avoids that the first substrate is directly exposed to the gas flow which enters the space. An embodiment of the method according to the invention in a device analogous to that shown in FIGS. 4 and 5 will now be described hereinafter.
On a platform having 20 supports of oxidized silicon, 19 supports of gallium arsenide are provided. The dimensions of the supports are 40 X 40 mm and the mutual intermediate space d between the adjacent supports varies from 10 to 20 mm according to a substantially linear arithmetical series. The platform with its charge is placed in a tubular reactor having inside cross-sections of X 40 mm, two passages of 40 X 15 mm being left free for the flow of the gas mixture on either side of the supports. The platform is directed so that the first support which does not support a substrate is present on the side of the gas supply which is also that of the minimum mutual intermediate space d.
The reactor is purified by means of hydrogen and then heated to the desired temperature, from which instant the substrates are maintained at a temperature between 750 and 800C with a gradient of 10 between the various substrate ends. A gas mixture containing the elements which are to be deposited, including the possible doping elements, and diluted with hydrogen and heated to a temperature of approximately 900C'is conveyed to the platform with substrates with a total supply in the order to 10 liters per minute.
A deposit of gallium arsenide phosphide carried out in these conditions and having an average thickness of 60 micrometers shows a maximum difference of 5% between the thicknesses deposited on the various substrates, as well as a difference of less than 20% between the concentrations of doping impurities.
What is claimed is:
l. A method of forming a deposit on a large number of flat substrates by reaction of a gaseous mixture of compounds of the elements to be deposited, said method comprising passing a gas flow containing gaseous compounds of the elements to be deposited through the zone of a tubular space containing the substrates arranged with their flat surfaces substantially perpendicular to the direction of the gas flow and each substrate being separated from the next substrate by a distance that increases in the direction of the flow of the gas, said gas being heated to a temperature above that of said substrates and depositing said elements on said substrates.
2. A method as claimed in claim 1, characterized in that each substrate is secured on a thin and flat support which has an area which is larger than that of the substrate secured thereto.
3. A method as claimed in claim 2, characterized in that each support supports only one substrate on one surface, all the substrates with their receiving surface being directed in the same direction as the gas flow.
4. A method as claimed in claim 1, characterized in that all the substrates are directed so that their receiving surfaces are directed towards the inlet of the gas flow in the space, the first support reached by the gas mixture supporting no substrate.
5. The method of claim 4 wherein the increase of the distances between substrates is substantially linear.
6. A flat crystalline semiconductor plate having a deposit obtained by the method of claim 1.

Claims (6)

1. A METHOD OF FORMING A DEPSIT ON A LARGE NUMBER OF FLAT SUBSTRATES BY REACTION OF A GASEOUS MIXTURE OF COMPOUNDS OF THE ELEMENS TO BE DEPOSITED, SAID METHOD COMPRISING PASSING A GAS FLOW CONTAINING GASEOUS COMPOUNDS OF THE ELEMENTS TO BE DEPOSITED THROUGH THE ZONE OF A TUBULAR SPACE CONTAINING THE SUBSTRATES ARRANGED WITH THEIR FLAT SURFACES SUBSTANTIALLY PERPENDICULAR TO THE DIRECTION OF THE GAS FLOW AND EACH SUBSTRAE BEING SEPARATED FROM THE NEXT SUBSTRATE BY A DISTANCE THAT INCREASES IN THE DIRECTION OF THE FLOW OF THE GAS, SAID GAS
2. A method as claimed in claim 1, characterized in that each substrate is secured on a thin and flat support which has an area which is larger than that of the substrate secured thereto.
3. A method as claimed in claim 2, characterized in that each support supports only one substrate on one surface, all the substrates with their receiving surface being directed in the same direction as the gas flow.
4. A method as claimed in claim 1, characterized in that all the substrates are directed so that their receiving surfaces are directed towards the inlet of the gas flow in the space, the first support reached by the gas mixture supporting no substrate.
5. The method of claim 4 wherein the increase of the distances between substrates is substantially linear.
6. A flat crystalline semiconductor plate having a deposit obtained by the method of claim 1.
US464574A 1973-04-27 1974-04-26 Vapour-phase deposition method Expired - Lifetime US3922467A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR7315461A FR2227640B1 (en) 1973-04-27 1973-04-27

Publications (1)

Publication Number Publication Date
US3922467A true US3922467A (en) 1975-11-25

Family

ID=9118616

Family Applications (1)

Application Number Title Priority Date Filing Date
US464574A Expired - Lifetime US3922467A (en) 1973-04-27 1974-04-26 Vapour-phase deposition method

Country Status (9)

Country Link
US (1) US3922467A (en)
JP (1) JPS5314464B2 (en)
AU (1) AU6831374A (en)
BE (1) BE814192A (en)
DE (1) DE2418662A1 (en)
FR (1) FR2227640B1 (en)
GB (1) GB1460758A (en)
IT (1) IT1010097B (en)
NL (1) NL7405442A (en)

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4082865A (en) * 1976-11-19 1978-04-04 Rca Corporation Method for chemical vapor deposition
US4096822A (en) * 1975-09-29 1978-06-27 Nippondenso Co., Ltd. Gaseous atmosphere control apparatus for a semiconductor manufacturing system
US4179326A (en) * 1976-04-22 1979-12-18 Fujitsu Limited Process for the vapor growth of a thin film
US4211821A (en) * 1976-06-14 1980-07-08 Agence Nationale De Valorisation De La Recherche (Anvar) Monocrystalline like layers, processes of manufacturing such layers, and articles comprising such layers
US4220116A (en) * 1978-10-30 1980-09-02 Burroughs Corporation Reactant gas flow structure for a low pressure chemical vapor deposition system
US4225647A (en) * 1977-12-02 1980-09-30 Parent Richard A Articles having thin, continuous, impervious coatings
US4263872A (en) * 1980-01-31 1981-04-28 Rca Corporation Radiation heated reactor for chemical vapor deposition on substrates
US4279947A (en) * 1975-11-25 1981-07-21 Motorola, Inc. Deposition of silicon nitride
US4355974A (en) * 1980-11-24 1982-10-26 Asq Boats, Inc. Wafer boat
US4401689A (en) * 1980-01-31 1983-08-30 Rca Corporation Radiation heated reactor process for chemical vapor deposition on substrates
US4574093A (en) * 1983-12-30 1986-03-04 At&T Bell Laboratories Deposition technique
US4640223A (en) * 1984-07-24 1987-02-03 Dozier Alfred R Chemical vapor deposition reactor
US4834022A (en) * 1985-11-08 1989-05-30 Focus Semiconductor Systems, Inc. CVD reactor and gas injection system
US4993358A (en) * 1989-07-28 1991-02-19 Watkins-Johnson Company Chemical vapor deposition reactor and method of operation
US20040060518A1 (en) * 2001-09-29 2004-04-01 Cree Lighting Company Apparatus for inverted multi-wafer MOCVD fabrication
US20110309562A1 (en) * 2010-06-18 2011-12-22 Tokyo Electron Limited Support structure and processing apparatus
JP2015145317A (en) * 2014-01-31 2015-08-13 ヤマハ株式会社 Device for producing carbon nanotube
US20150275360A1 (en) * 2014-03-25 2015-10-01 Tokyo Electron Limited Vacuum Processing Apparatus

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53126271A (en) * 1977-04-11 1978-11-04 Kokusai Electric Co Ltd Reduced pressure gaseous growing method and boarding jig
NL7812388A (en) * 1978-12-21 1980-06-24 Philips Nv METHOD FOR MANUFACTURING A SEMI-CONDUCTOR DEVICE AND SEMI-CONDUCTOR DEVICE MADE USING THE METHOD
KR830002904Y1 (en) * 1982-06-16 1983-12-13 채이순 Car Watering Mad
JPS6223983A (en) * 1985-07-25 1987-01-31 Anelva Corp Vacuum chemical reactor
FR2604297B1 (en) * 1986-09-19 1989-03-10 Pauleau Yves SILICON DOPE DEPOSIT REACTOR
JPS63162862U (en) * 1988-03-16 1988-10-24

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3409483A (en) * 1964-05-01 1968-11-05 Texas Instruments Inc Selective deposition of semiconductor materials
US3678893A (en) * 1970-05-01 1972-07-25 Stewart Warner Corp Improved device for supporting semiconductor wafers
US3816166A (en) * 1970-03-11 1974-06-11 Philips Corp Vapor depositing method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3409483A (en) * 1964-05-01 1968-11-05 Texas Instruments Inc Selective deposition of semiconductor materials
US3816166A (en) * 1970-03-11 1974-06-11 Philips Corp Vapor depositing method
US3678893A (en) * 1970-05-01 1972-07-25 Stewart Warner Corp Improved device for supporting semiconductor wafers

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4096822A (en) * 1975-09-29 1978-06-27 Nippondenso Co., Ltd. Gaseous atmosphere control apparatus for a semiconductor manufacturing system
US4279947A (en) * 1975-11-25 1981-07-21 Motorola, Inc. Deposition of silicon nitride
US4179326A (en) * 1976-04-22 1979-12-18 Fujitsu Limited Process for the vapor growth of a thin film
US4211821A (en) * 1976-06-14 1980-07-08 Agence Nationale De Valorisation De La Recherche (Anvar) Monocrystalline like layers, processes of manufacturing such layers, and articles comprising such layers
US4082865A (en) * 1976-11-19 1978-04-04 Rca Corporation Method for chemical vapor deposition
US4225647A (en) * 1977-12-02 1980-09-30 Parent Richard A Articles having thin, continuous, impervious coatings
US4220116A (en) * 1978-10-30 1980-09-02 Burroughs Corporation Reactant gas flow structure for a low pressure chemical vapor deposition system
US4401689A (en) * 1980-01-31 1983-08-30 Rca Corporation Radiation heated reactor process for chemical vapor deposition on substrates
US4263872A (en) * 1980-01-31 1981-04-28 Rca Corporation Radiation heated reactor for chemical vapor deposition on substrates
US4355974A (en) * 1980-11-24 1982-10-26 Asq Boats, Inc. Wafer boat
US4574093A (en) * 1983-12-30 1986-03-04 At&T Bell Laboratories Deposition technique
US4640223A (en) * 1984-07-24 1987-02-03 Dozier Alfred R Chemical vapor deposition reactor
US4834022A (en) * 1985-11-08 1989-05-30 Focus Semiconductor Systems, Inc. CVD reactor and gas injection system
US4993358A (en) * 1989-07-28 1991-02-19 Watkins-Johnson Company Chemical vapor deposition reactor and method of operation
US20040060518A1 (en) * 2001-09-29 2004-04-01 Cree Lighting Company Apparatus for inverted multi-wafer MOCVD fabrication
US8133322B2 (en) 2001-09-29 2012-03-13 Cree, Inc. Apparatus for inverted multi-wafer MOCVD fabrication
US20110309562A1 (en) * 2010-06-18 2011-12-22 Tokyo Electron Limited Support structure and processing apparatus
JP2015145317A (en) * 2014-01-31 2015-08-13 ヤマハ株式会社 Device for producing carbon nanotube
US20150275360A1 (en) * 2014-03-25 2015-10-01 Tokyo Electron Limited Vacuum Processing Apparatus

Also Published As

Publication number Publication date
JPS5314464B2 (en) 1978-05-17
IT1010097B (en) 1977-01-10
FR2227640B1 (en) 1977-12-30
AU6831374A (en) 1975-10-30
JPS5016476A (en) 1975-02-21
GB1460758A (en) 1977-01-06
NL7405442A (en) 1974-10-29
DE2418662A1 (en) 1974-11-21
BE814192A (en) 1974-10-25
FR2227640A1 (en) 1974-11-22

Similar Documents

Publication Publication Date Title
US3922467A (en) Vapour-phase deposition method
US3672948A (en) Method for diffusion limited mass transport
US3805736A (en) Apparatus for diffusion limited mass transport
US4082865A (en) Method for chemical vapor deposition
US5700520A (en) Low temperature, high pressure silicon deposition method
US5874129A (en) Low temperature, high pressure silicon deposition method
US5221556A (en) Gas injectors for reaction chambers in CVD systems
US4421786A (en) Chemical vapor deposition reactor for silicon epitaxial processes
KR20020070161A (en) Chemical vapor deposition apparatus and chemical vapor deposition method
US4732110A (en) Inverted positive vertical flow chemical vapor deposition reactor chamber
EP1193331B1 (en) Chemical vapor deposition apparatus and chemical vapor deposition method
US3682699A (en) Method of vapor growth of a semiconductor crystal
US4466381A (en) Coating of semiconductor wafers and apparatus therefor
EP0353256B1 (en) Method of purifying and depositing group iiib and group vb compounds to produce epitaxial films
US3413145A (en) Method of forming a crystalline semiconductor layer on an alumina substrate
EP0031671B1 (en) A method of growing silicate glass layers employing a chemical vapour deposition process
US3089788A (en) Epitaxial deposition of semiconductor materials
US4389273A (en) Method of manufacturing a semiconductor device
US3524776A (en) Process for coating silicon wafers
US3304908A (en) Epitaxial reactor including mask-work support
EP0437355B1 (en) Process and apparatus for preparing a thin film electroluminescent device
US3341374A (en) Process of pyrolytically growing epitaxial semiconductor layers upon heated semiconductor substrates
JPS6171625A (en) Vertical cvd device
JPS61501237A (en) Deposition technology
GB2213836A (en) Vacuum deposition process