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WO2008032752A1 - Substrate production equipment - Google Patents

Substrate production equipment Download PDF

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Publication number
WO2008032752A1
WO2008032752A1 PCT/JP2007/067767 JP2007067767W WO2008032752A1 WO 2008032752 A1 WO2008032752 A1 WO 2008032752A1 JP 2007067767 W JP2007067767 W JP 2007067767W WO 2008032752 A1 WO2008032752 A1 WO 2008032752A1
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WO
WIPO (PCT)
Prior art keywords
gas
hole
inert gas
chamber
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.)
Ceased
Application number
PCT/JP2007/067767
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French (fr)
Japanese (ja)
Inventor
Kenji Yasutake
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.)
Sharp Corp
Original Assignee
Sharp Corp
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Filing date
Publication date
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Publication of WO2008032752A1 publication Critical patent/WO2008032752A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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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
    • C30B19/00Liquid-phase epitaxial-layer growth
    • C30B19/06Reaction chambers; Boats for supporting the melt; Substrate holders

Definitions

  • the present invention relates to a substrate manufacturing apparatus for manufacturing a thin plate substrate from a metal or semiconductor melt.
  • a method of manufacturing a thin plate-like substrate As a method of manufacturing a thin plate-like substrate, a crystal ribbon method and an EFG (Edge-defined Film-fed Growth) method are known.
  • the substrate manufacturing apparatus that realizes these methods has a drive unit provided outside the chamber in which crystal growth is performed, so there is an advantage that the apparatus becomes small! (See, for example, JP-A-2001-322892) .
  • the substrate is produced by crystal growth in a direction perpendicular to the thickness direction of the substrate rather than crystal growth in the thickness direction of the substrate! /
  • the problem is low! /, And! /
  • FIG. 9 is a cross-sectional view showing another conventional substrate manufacturing apparatus 101.
  • the substrate manufacturing apparatus 101 manufactures a substrate by immersing a plate-like cooling body 103 in a melt 102 of the substrate material and crystal-growing the melt 102 on the surface 103 a in the thickness direction of the cooling body 103. This increases the productivity of the substrate.
  • the substrate manufacturing apparatus 101 includes a crucible 111 that accommodates the melt 102, a transport means 104 that holds the cooling body 103 and is immersed in the melt 102, a channel 105 that houses the crucible 111 and the transport means 104, and a load lock.
  • the chamber 106 is configured to include a gate valve 107 and a vacuum pump 108. In FIG. 9, the moving direction of the conveying means 104 is indicated by an arrow 109.
  • the load lock chamber 106 is a load lock chamber for loading (positioned on the left side in FIG. 9) that passes when the cooling body 103 is loaded into the chamber 105, and is cooled outside the substrate manufacturing apparatus 101 from within the chamber 105. And a load lock chamber (located on the right side in FIG. 9) through which the cooling body 103 passes when the body 103 is unloaded.
  • the load lock chamber 106 for loading and unloading is separated from the chamber 105 by a gate valve 107, and is also shielded from outside air. The gate valve 107 is opened only when the cooling body 103 passes.
  • Inside the chamber 105 and the load lock chamber 106 for loading and unloading The inside is evacuated by a vacuum pump 108 and an inert gas is supplied into the chamber 105. In FIG. 9, the flow direction of the inert gas is indicated by an arrow 110.
  • a substrate manufacturing apparatus 101 it becomes necessary to provide a driving unit such as a conveying means 104 for transporting the cooling body 103 at a predetermined path and speed in the chamber 105, and the chamber becomes larger.
  • a driving unit such as a conveying means 104 for transporting the cooling body 103 at a predetermined path and speed in the chamber 105
  • the chamber becomes larger.
  • the substrate can be grown in the thickness direction of the substrate from the surface of the cooling body 103, the manufacturing speed of the substrate can be increased. In this way, a substrate manufacturing apparatus with high substrate productivity is realized (see, for example, Japanese Patent Application Laid-Open No. 2004 161583).
  • the concentration of chemically active oxygen or the like increases in the chamber 105, impurities are mixed into the melt 102, which is a material of the substrate, and a substrate having a high quality in terms of purity and crystallinity can be manufactured. Can not. Therefore, in the conventional substrate manufacturing apparatus 101 described above, the inside of the chamber 105 is evacuated, and an inert gas is supplied into the chamber 105 to eliminate oxygen and the like. Equipment for vacuum environment such as load lock chamber 106, gate valve 107 and vacuum pump 108 is required. Since an apparatus for a vacuum environment is required in this way, there arises a problem that the substrate manufacturing apparatus 101 is complicated and enlarged, the installation area is increased, and the cost of the substrate manufacturing apparatus 101 is increased.
  • the crucible 111 containing the melt 102 of the metal material or the semiconductor material is formed using quartz glass or carbon in order to prevent contamination of the material forming the crucible 111 with the melt 102.
  • the disposable crucible 111 since carbon is lower in cost than quartz glass, it is often formed using carbon.
  • drive devices such as the transport means 104 provided in the chamber 105 are often formed using a single bonnet.
  • the crucible 111 formed of carbon and the driving device are worn out. There is a problem. Therefore, in the conventional substrate manufacturing apparatus 101, in order to reduce the concentration of oxygen in the chamber 105, oxygen in the chamber 105 is excluded by using a vacuum environment apparatus. The manufacturing apparatus 101 becomes complicated and large, so that the installation area increases, and the cost of the board manufacturing apparatus 101 increases. Disclosure of the invention
  • an object of the present invention is to provide a substrate manufacturing apparatus capable of reducing the oxygen concentration in a chamber with a simple configuration.
  • the present invention is a substrate manufacturing apparatus for manufacturing a substrate by immersing a cooling body in a melt obtained by heating and melting a raw material of a substrate, and solidifying and growing the raw material on a surface of the cooling body.
  • a chamber that includes a crucible for storage, and that forms a storage space in which the crucible is stored;
  • Gas supply means for supplying an inert gas to the accommodation space
  • a communication hole that communicates with the housing space and allows the cooling body to pass therethrough, an exhaust hole that exhausts gas, and a transport hole that communicates with the external space and allows the cooling body to pass therethrough are formed.
  • a conveying means for carrying the cooling body into the accommodation space through the communication hole and the conveyance hole and carrying out the cooling body from the accommodation space;
  • a substrate manufacturing apparatus including gas ejection means for ejecting an inert gas toward a cooling body accommodated in the buffer space and conveyed through the buffer space by the conveyance means.
  • the present invention also includes a plurality of the buffer chambers,
  • the gas supply means supplies the inert gas to the accommodation space so that the flow rates of the inert gas flowing into the buffer spaces through the communication holes of the buffer chambers become equal.
  • the volume of the buffer chamber is selected to be more than 0% and 10% or less of the volume of the chamber.
  • the gas ejection means is provided in the buffer space close to the transport hole. It is characterized by that.
  • the present invention is characterized in that the opening / closing means is provided in the vicinity of the transport hole. Also, the invention is characterized in that the gas ejection means ejects an inert gas toward the exhaust hole. To do.
  • the present invention is characterized in that the gas jetting means jets gas over the outside of the region into a region surrounded by a virtual surface extending the surface defining the transport hole.
  • the gas ejection means is formed to extend in a predetermined direction perpendicular to the direction in which the inert gas is ejected, and has an ejection hole through which the inert gas is ejected.
  • the width dimension of the ejection hole in the gas ejection direction and the direction perpendicular to the predetermined direction is selected to be 0.05 mm or more and less than 0.2 mm.
  • the present invention is characterized in that the gas jetting means jets an inert gas in a direction parallel to a surface of a cooling body for solidifying and growing the raw material.
  • the present invention is characterized in that the inert gas ejected from the gas ejection means is selected from at least one of a rare gas and a nitrogen gas.
  • FIG. 1 is a cross-sectional view schematically showing a configuration of a substrate manufacturing apparatus 1 according to an embodiment of the present invention.
  • FIG. 2 is an enlarged cross-sectional view of section II of FIG.
  • FIG. 3 is a cross-sectional view of the buffer chamber 6 as seen from the section line III-III in FIG.
  • FIG. 4 is a diagram showing the relationship between the flow rate of the inert gas ejected from the gas ejection means 35 and the oxygen concentration in the accommodation space 9.
  • FIG. 5 is a diagram showing the relationship between the chamber flow rate and the oxygen concentration in the accommodation space 9.
  • FIG. 6 is a cross-sectional view of the buffer chamber 6 when the gas ejection means 35 is provided on the one side wall 39 in the first direction X of the buffer chamber body 19.
  • FIG. 7 is a cross-sectional view of a buffer chamber 6 of a substrate manufacturing apparatus 1 according to another embodiment of the present invention.
  • FIG. 8 is a cross-sectional view illustrating a substrate manufacturing apparatus 51 according to still another embodiment of the present invention.
  • FIG. 9 is a cross-sectional view showing another conventional substrate manufacturing apparatus 101.
  • FIG. 1 is a cross-sectional view schematically showing a configuration of a substrate manufacturing apparatus 1 according to an embodiment of the present invention.
  • a substrate manufacturing apparatus 1 includes a crucible 2 and carries a chamber 3 that forms a storage space 9 in which the crucible 2 is stored, and a cooling body (hereinafter also referred to as a base plate) 4 in the storage space 9.
  • the substrate manufacturing apparatus 1 immerses the plate-like base plate 4 in the melt 11 to solidify and grow the melt 11 on the one surface 4 a in the thickness direction of the base plate 4 to manufacture the substrate 12.
  • the substrate manufacturing apparatus 1 is used to manufacture a low-cost thin-plate silicon substrate used for, for example, a solar cell.
  • the chamber 3 further includes heating means provided so as to surround the crucible 2.
  • the heating means is realized by a resistance heating device, an induction heating device, or the like.
  • the heating means melts the raw material of the substrate 12 by heating the raw material of the solid substrate 12 filled in the crucible 2 to a high temperature equal to or higher than the melting point.
  • the raw material of the substrate 12 is made of, for example, a metal material and a semiconductor material.
  • the crucible 2 contains a liquid melt 11 melted by a heating means. In the present embodiment, crucible 2 is formed containing carbon.
  • the transport means 5 transports the base plate 4 and immerses it in the melt 11.
  • the transporting means 5 is arranged on one side of the crucible 2 in the vertical direction Z (hereinafter referred to as the upper Z1) when the substrate manufacturing apparatus 1 is in use.
  • the transport means 5 includes a shaft body 18 that is rotatably supported around a first axis L1 parallel to a predetermined first direction X perpendicular to the vertical direction Z in the storage space 9, and a shaft 18 to the first axis. And a plurality of arms 13 extending outward in the radial direction centered on L1. Multiple arms 13 are centered on the first axis L1.
  • each arm 13 is shown as an example.
  • An outer end portion in the radial direction around the first axis L1 of each arm 13 constitutes a holding portion 14 that holds the base plate 4.
  • the holding portion 14 has a shape that fits with the base plate 4.
  • the holding portion 14 is formed with a groove between both end portions in the circumferential direction centered on the first axis L1, and the other surface portion in the thickness direction of the base plate 4 is perpendicular to the thickness direction.
  • a convex groove extending in any direction is formed, and the convex groove and the concave groove are fitted.
  • the cross section perpendicular to the direction in which the groove extends is trapezoidal, and the longer lower base is formed closer to the shaft body 18 than the shorter upper base.
  • a lower base that is slightly smaller than the cross section of the concave grooves and longer than the upper base is formed at the other end in the thickness direction.
  • the arm 13 holds the base plate 4 by fitting the convex groove of the base plate 4 and the concave groove of the holding portion 14 into each other.
  • the transport means 5 is configured to include carbon.
  • the length of the arm 13 is adjusted so that one surface portion in the thickness direction of the base plate 4 is immersed in the melt 11 when the arm 13 is parallel to the vertical direction Z. Is set. Further, when the arm 13 is parallel to the vertical direction Z, the arm 13 holds the base plate 4 so that one surface 4a in the thickness direction of the base plate 4 is parallel to the liquid surface of the melt 11. .
  • the substrate manufacturing apparatus 1 further includes gas supply means 15 that supplies an inert gas to the accommodation space 9.
  • the inert gas supplied by the gas supply means 15 is selected from rare gases such as argon and helium and nitrogen gas, for example.
  • the gas supply means 15 has a gas supply pipe connected to one or a plurality of inert gas inflow holes 16 formed in the upper wall portion of the upper Z1 of the chamber 3.
  • the gas supply means 15 supplies the inert gas to the chamber 3 through the inert gas inflow hole 16.
  • two inert gas inflow holes 16 are provided in the upper wall portion of the chamber 3, and the inert gas is supplied from the two inert gas inflow holes 16.
  • the gas supply means 15 supplies an inert gas with an equal flow rate from the inert gas inflow holes 16 to the accommodation space 9.
  • the gas such as oxygen flowing into the accommodation space 9 can be exhausted from the chamber 3, and the substrate 12 can be manufactured in an inert gas atmosphere.
  • the substrate 12 is manufactured in an inert gas atmosphere, it is possible to prevent the melt 11 from reacting with oxygen in the atmosphere and mixing impurities into the substrate 12. Further, it is possible to suppress the transport means 5 and the crucible 2 from being oxidized and consumed.
  • the flow of the inert gas in the substrate manufacturing apparatus 1 is indicated by an arrow F1.
  • the chamber 3 is formed symmetrically with respect to a predetermined second axis L2 parallel to the vertical direction Z. Accordingly, the two inert gas inflow holes 16 formed in the chamber 3 are also formed symmetrically with respect to the predetermined second axis L2.
  • the gas supply means 15 supplies the inert gas having the same flow rate from the inert gas inflow holes 16 to the storage space 9, so that the inert gas flowing through the storage space 9 is also determined in advance by the second axis L2 Flows symmetrically with respect to.
  • the transport means 5 further includes drive means for rotationally driving the shaft body 18 while angularly displacing the shaft body 18 to one F2 around the first axis L1.
  • Each arm 13 rotates together with the shaft 18 that is driven to rotate by the driving means while holding the base plate 4 that is conveyed by the conveying means 7.
  • each arm 13 rotates counterclockwise around the first axis L1.
  • the base plate 4 held by the arm 13 is immersed in the melt 11 while the base plate 4 is immersed in the melt from one surface 4a in the thickness direction.
  • Substrate 12 is formed by solidification growth of 11.
  • the thickness of the substrate 12 formed on the base plate 4 depends on the temperature of the melt 11 and the rotational speed of the shaft 18.
  • the temperature of the melt 11 and the rotational speed of the shaft 18 are controlled by control means realized including a central processing unit (abbreviated as CPU).
  • CPU central processing unit
  • An opening communicating with the buffer chamber 6 is formed in the chamber 3.
  • the base plate 4 is carried into the accommodation space 9 through this opening or carried out of the accommodation space 9.
  • the gas in the storage space 9 is exhausted out of the storage space 9 through this opening.
  • FIG. 2 is an enlarged cross-sectional view of section II in FIG.
  • the buffer chamber 6 includes a first buffer chamber (located on the left side in FIG. 1) through which the base plate 4 passes when the base plate 4 is carried into the storage space 9, and a base plate 4 when the base plate 4 is carried out of the storage space 9. Second buffer chamber ( Figure) 1 on the right side). Since the first and second buffer chambers 6 have the same structure and are arranged symmetrically with respect to the above-described predetermined second axis L2, the first and second buffer chambers 6 will be described together.
  • the buffer chamber 6 includes a buffer chamber main body 19 that forms a buffer space 25, a communication pipe 20 that extends from the one side wall 29 facing the chamber 3 of the buffer chamber main body 19 to the chamber 3, and a communication pipe 20 of the buffer chamber main body 19.
  • a transfer pipe 21 extending from the other side wall 30 facing the provided side wall 29 to the opposite side of the chamber 3, and an upper wall 31 of the upper Z1 of the buffer chamber body 19 extending from the upper wall 31 to the upper Z1 and connected to the exhaust pipe 8.
  • Connecting pipe 22 is provided to the exhaust pipe 8.
  • a pipe line (hereinafter referred to as a communication hole) 17 formed by the communication pipe 20 communicates with the accommodation space 9 through an opening formed in the chamber 3, and the buffer space 25 communicates with the accommodation space 9 through the communication hole 17. .
  • the inert gas supplied from the gas supply means 15 flows symmetrically with respect to the predetermined second axis L2, the inert gas flowing into the buffer spaces 25 through the communication holes 17 respectively.
  • the gas flow is equal.
  • the flow rate of the inert gas flowing through one or more specific communication holes 17 out of the plurality of communication holes 17 is small, the force S that makes it easy for outside air to flow into the accommodation space 9 from the communication holes 17 with a low flow rate. Since the flow rates of the inert gas flowing through the communication hole 17 are the same, it is possible to prevent outside air from flowing into the accommodation space 9 from the buffer space 25. This reduces the oxygen concentration in the accommodation space 9 by the force S.
  • the base plate 4 is carried into the buffer space 25 from the outside of the substrate manufacturing apparatus 1 through the pipe line (hereinafter referred to as “transport hole”) 23 formed by the transport pipe 21, or the buffer space 25 through the transport hole 23. From outside the board manufacturing apparatus 1.
  • the substrate manufacturing apparatus 1 further includes opening / closing means 24 that can open and close the transport hole 23.
  • the opening / closing means 24 is provided close to the end of the buffer chamber 6 opposite to the chamber 3 side, that is, the end of the transfer tube 21 opposite to the buffer chamber body 19 side.
  • the opening / closing means 24 includes a thin rectangular parallelepiped or plate-shaped shirt 33 capable of opening and closing the transport hole 23, an air cylinder provided above Z1 of the shirt 33, a rod connecting the shirt 33 and the air cylinder, and the shirt 33 And a linear guide that regulates movement.
  • the shirt 33 is formed of a metal material and a resin material.
  • the shirtta 33 is the one that removes the vertical direction Z by the linear guide.
  • Movement in the direction is restricted, and it can be moved only in the vertical direction Z.
  • the air cylinder presses or pulls the shirt 33 in the vertical direction Z through the mouth the shirt 33 moves in the vertical direction Z.
  • the transport hole 23 is opened and closed by moving the shirt 33 in the vertical direction Z.
  • the shirter 33 is formed so that a cross section perpendicular to the thickness direction is at least larger than a cross section of the transport hole 23 perpendicular to the direction in which the transport pipe 21 extends, and when viewed in one of the thickness directions of the shirter 33 when moved downward Z2. It is formed in a shape that covers the transport hole 23.
  • the shirt 33 moves to the upper Z1 to open the transport hole 23, and otherwise moves to the lower Z2 to close the transport hole 23. .
  • the opening / closing means 24 is provided close to the transport pipe 21, that is, close to the transport hole 23, the gap between the open / close means 24 and the transport hole 23 is narrowed. Therefore, gas such as air can be prevented from flowing into the accommodation space 9 from this gap. As a result, the oxygen concentration in the accommodation space 9 can be reduced, impurities can be prevented from being mixed into the substrate 4, and the life of the substrate manufacturing apparatus 1 can be extended.
  • connection pipe 22 extends upward Z1 from the end of the upper wall 31 of the buffer chamber body 19 opposite to the chamber 3 side.
  • the exhaust pipe 8 extends from the connecting pipe 22 formed in each buffer chamber 6 to the upper Z1, and is connected to the upper Z1 of the chamber 3 from the end of the upper Z1. It is formed extending horizontally.
  • An opening 27 is formed in the upper wall of Z1 above the connecting portion 26 of the exhaust pipe 8.
  • the inert gas supplied from the gas supply means 15 to the chamber 3 is formed by the chamber 3, the communication hole 17, the buffer space 25, a pipe line (hereinafter referred to as an exhaust hole) 34 formed by the connection pipe 22, and the exhaust pipe 8. Then, the air is exhausted out of the substrate manufacturing apparatus 1 through the pipe line and the opening 27 formed in the connecting portion 26 of the exhaust pipe 8 in this order.
  • the volume of the buffer chamber 6, that is, the volume of the buffer space 25, the volume of the communication hole 17, the volume of the transfer hole 23, and the volume of the exhaust hole 34 is the volume of the chamber 3. That is, it is selected to exceed 0% and not more than 10% of the volume of the accommodating space 9. Since the inert gas supplied from the gas supply means 15 flows into the buffer space 25 from the storage space 9, the pressure in the buffer space 25 is at least higher than the atmospheric pressure. If the pressure in the buffer space 25 is higher than atmospheric pressure, the outside air will be in the buffer space 25 when the transfer hole 23 is open. Can be prevented.
  • the volume of the buffer chamber 6 When the volume of the buffer chamber 6 is larger than 10% of the volume of the chamber 3, the effect of increasing the pressure in the buffer space 25 is reduced, so the difference between the atmospheric pressure and the pressure in the buffer space 25 is reduced. The effect of preventing outside air from flowing into the buffer space 25 is reduced. If the volume of the buffer chamber 6 is sufficiently smaller than the volume of the chamber 3 as in the present embodiment, the difference between the pressure in the buffer space 25 and the atmospheric pressure is larger than when the volume of the buffer chamber 6 is large. It becomes large and can effectively prevent outside air from flowing into the buffer chamber 6. As a result, the oxygen concentration in the buffer space 25 can be reduced, and accordingly, the oxygen concentration in the accommodation space 9 can be reduced.
  • the transport means 7 transports the base plate 4 carried into the buffer chamber 6 to the transport means 5 provided in the accommodation space 9, or transports the base plate 4 transported by the transport means 5 to the buffer chamber 6.
  • the conveying means 7 includes, for example, two rails extending in parallel, a plurality of shafts extending in a direction perpendicular to the extending direction of the two rails and having both ends pivotally supported by the rails, and shafts on the shafts.
  • a plurality of transport rollers that are supported and are arranged at equal intervals in the axial direction of the shaft, and a drive body that rotationally drives each shaft around the axis. Each shaft is arranged at equal intervals in the extending direction of the two rails.
  • Each shaft is provided with three or more disk-shaped transport rollers, and each transport roller rotates together with the shaft.
  • an inert gas is ejected from the gas ejection means 35 to the transport means 7 from the lower Z2 toward the upper Z1.
  • the conveying roller and the shaft are arranged at a sufficient interval so as not to disturb the flow of the inert gas from the gas ejection means 35.
  • the conveying means 7 conveys the base plate 4 placed on the conveying roller from the upper Z1 of the conveying means 7 in the direction in which the two rails extend as each shaft rotates.
  • the conveying direction of the base plate 4 is switched depending on the rotation direction of the shaft.
  • the base plate 4 transported to the transport means 5 by the transport means 7 is fitted and held in the holding portion 14 of the transport means 5 as described above, and is immersed in the melt 11 by the transport means 5 and transported by the transport means 7. And is further transported to the buffer chamber 6 by the transport means 7.
  • FIG. 3 is a cross-sectional view of the buffer chamber 6 as seen from the section line III III in FIG.
  • the substrate manufacturing apparatus 1 further includes gas ejection means 35 in the buffer space 25.
  • the gas ejection means 35 is provided in the buffer space 25 close to the transport hole 23.
  • the gas jetting means 35 is provided at the end near the transfer pipe 21 on the lower wall 36 of the lower Z2 of the buffer chamber body 19.
  • the gas ejection means 35 extends along the other side wall 30 between both ends of the first direction X perpendicular to the up-down direction Z of the other side wall 30.
  • An ejection hole extending between both end portions in the first direction X is formed at the end portion of the upper Z1 of the gas ejection means 35.
  • the gas ejection means 35 includes an inert gas supply source that supplies an inert gas to the ejection hole, and ejects the inert gas from the ejection hole toward the upper Z1.
  • the ejection hole of the gas ejection means 35 is a long hole that is long in the extending direction of the gas ejection means 35 (first direction X), and the inner peripheral surface facing this ejection hole is a square. It has a cylindrical shape.
  • the flow of the inert gas ejected from the gas ejection hole is indicated by an arrow 38.
  • connection pipe 22 is provided at the end of the upper wall 31 of the buffer chamber body 19 near the transport pipe 21, the gas ejection means 35 is located below the exhaust hole 34 at Z2 and is connected to the exhaust hole 34. Inert gas is spouted out.
  • the transport pipe 21 described above has a rectangular cylindrical shape, and an opening 37 through which the transport hole 23 communicates is formed on the other side wall 30 of the buffer chamber body 19.
  • This opening 37 extends in the first direction X in the same manner as the direction in which the gas ejection means 35 extends, and is located above the gas ejection means 35 when viewed from one of the vertical direction Z and the second direction Y perpendicular to the first direction X. Formed in Z1.
  • the opening 37 is formed in the center of the gas ejection hole in the first direction X.
  • the width dimension W1 in the extending direction of the gas ejection holes (hereinafter referred to as the dimension W1 in the longitudinal direction of the gas ejection holes) is the width dimension in the extending direction of the gas ejection means 35 of the opening 37 formed in the other side wall 30. It is selected to be larger than W2 (hereinafter referred to as the dimension W2 in the longitudinal direction of the opening 37), preferably 1.5 times the dimension W2 in the longitudinal direction of the opening 37. That is, the gas ejection means 35 is in a region (a region in the opening 37 in FIG. 3) surrounded by a virtual plane that is an extension of the inner peripheral surface of the transport pipe 21 that faces the transport hole 23, that is, the transport hole 23.
  • the gas is ejected to the outside of the region. Since the flow of the inert gas ejected from the gas ejection hole is disturbed at the end in the extending direction of the gas ejection hole, if the gas is ejected only to the region, the part of the inert gas flow is disturbed. However, the outside air flowing from the transfer hole 23 cannot be effectively exhausted to the exhaust hole 34. Since the gas jetting means 35 jets the gas to the outside of the area, there is no turbulence in the flow of inert gas in the area, and the outside air flowing in from the transfer hole 23 is more effective. The exhaust hole 34 can be exhausted. As a result, the outside air can be prevented from flowing into the accommodation space 9 through the communication hole 17 and the oxygen concentration in the accommodation space 9 can be reduced.
  • the base plate 4 passes through the upper Z1 of the gas ejection means 35 when it is carried into the buffer space 25 through the conveyance hole 23 by the conveyance means 7.
  • the gas ejection means 35 ejects the inert gas toward the base plate 4 passing through the upper Z1, the outside air that covers and covers the base plate 4 is separated from the base plate 4.
  • the oxygen gas 28 is schematically indicated by the symbol “ ⁇ ”, and the direction in which the oxygen gas 28 flows by the inert gas ejected from the gas ejection means 35 is indicated by an arrow 32.
  • the gas ejection means 35 is provided in the buffer space 25 close to the transport hole 23.
  • the gas jetting means 35 jets an inert gas to the base plate 4 in the buffer space 25 and in the vicinity of the transport hole 23 that is close to the communication hole 17.
  • oxygen and other gases covering the base plate 4 are separated from each other at a position away from the communication hole 17, so that it is possible to prevent the separated gas from passing through the communication hole 17 as much as possible, and the outside air enters the accommodation space 9. It can be prevented from flowing. This reduces the oxygen concentration in the accommodation space 9 by the force S.
  • the gas ejection means 35 is located in the lower Z2 of the exhaust hole 34 and ejects the inert gas toward the exhaust hole 34, so that the inert gas swirls in the buffer space 25,
  • the gas flows from the gas jetting means 35 to the exhaust hole 34 without stagnation, and a flow of inert gas is generated.
  • a gas such as oxygen separated from the base plate 4 can be smoothly conveyed to the exhaust hole 34.
  • it is possible to prevent the gas such as oxygen separated from the base plate 4 from flowing into the accommodation space 9 through the communication hole 17.
  • inert gas' A curtain This inert gas curtain has a function of transporting gas passing through itself to the communication hole 17.
  • the dimension in the second direction Y of the gas ejection hole of the gas ejection means 35 is preferably 0.05 mm or more and less than 0.2 mm. If the dimension of the gas injection hole in the second direction Y is less than 0.05 mm, the flow rate will be high when the flow rate is constant, so there will be little! /, And the inert gas will be used to efficiently blow the gas to the cooling body. Force that can be generated The pressure loss becomes large, and it becomes difficult for the inert gas to flow, and the flow rate of the inert gas in the direction in which the ejection holes extend becomes uneven.
  • the flow rate of the inert gas increases when the flow rate is high.
  • the production cost of the substrate becomes high due to the large amount of inert gas used.
  • the flow size of the ejection holes is controlled by setting the width dimension of the ejection holes to 0.05 mm or more and less than 0.2 mm, The force S is used to make the flow rate of the inert gas uniform in the direction in which the jet hole extends.
  • FIG. 4 is a diagram showing the relationship between the flow rate of the inert gas ejected from the gas ejection means 35 and the oxygen concentration in the accommodation space 9.
  • the horizontal axis represents the flow rate of the inert gas ejected from the gas ejection means 35 (hereinafter referred to as curtain flow rate), and the vertical axis represents the oxygen concentration in the accommodation space 9.
  • the measurement results of the oxygen concentration shown in FIG. 4 are measured values when the flow rate of the inert gas supplied from the gas supply means 15 to the accommodation space 9 (hereinafter referred to as the chamber flow rate) is 200 L / min. As shown in Fig.
  • the curtain flow rate is 100 L / min or more
  • the oxygen concentration in the containing space 9 can be kept at 5 ppm or less, so that the inert gas' curtain functions as a barrier that blocks outside air flowing into the containing space 9. Is shown to be particularly prominent
  • the curtain flow rate is selected to be 20 L / min or more, preferably 100 L / min or more.
  • the correlation between the curtain flow rate and the oxygen concentration in the accommodating space 9 is different. If the Reynolds number Re and the Schmidt number Sc defined in Eq. (1) and Eq. (2) are equal, the flow velocity distribution and concentration distribution are similar from the flow velocity and concentration distribution similarity rules. Therefore, it is estimated that the oxygen concentration in the accommodation space 9 depends on the Reikarez number Re and the Schmitt number Sc regardless of the shape of the substrate manufacturing apparatus 1.
  • the Reynolds number Re and the Schmidt number Sc are dimensionless numbers.
  • U represents the representative flow velocity (unit m / s)
  • L represents the representative length ⁇ 4 X opening area / opening circumference (unit m) ⁇
  • V is inert.
  • V represents the kinematic viscosity coefficient (unit m 2 / s) of gas.
  • V represents the kinematic viscosity coefficient (unit m 2 / s) of the inert gas
  • D represents the diffusion coefficient (unit m 2 / s) of oxygen to the inert gas. .
  • the Reikarezu number Re is the same, the oxygen concentration in the accommodation space 9 is estimated to be equal regardless of the shape of the substrate manufacturing apparatus 1. That is, even if the shape of the substrate manufacturing apparatus 1 is different, it is estimated that the correlation between the oxygen concentration in the accommodation space 9 and the Reikarezu number Re is the same. Since the Reikarezu number Re is determined from the oxygen concentration of the target accommodating space 9 and the representative length L is obtained from the shape of the substrate manufacturing apparatus 1, the force S for obtaining the representative flow velocity U from the equation (1) can be obtained. When the representative flow velocity U is obtained, the curtain flow rate to be ejected from the gas ejection means 35 can be determined.
  • the size of the gas ejection hole of the gas ejection means 35 is 500 mm X O. 1 mm.
  • the gas ejection when the curtain flow rate is l OOL / min. Reynolds number Re of means 35 (hereinafter referred to as curtain. Reynolds number Re)
  • the curtain Reynolds number Re is 92 when the curtain flow rate is 20L / min. Analyzing the above experimental results based on the curtain 'Reikarez number Re, when the curtain Reynolds number Re is 460 or more, the oxygen concentration in the containment space 9 is kept below 5 ppm due to the shielding effect of the inert gas curtain. It is.
  • the curtain “Reikarezu number Re” is selected to be 92 or more, and preferably 460 or more.
  • FIG. 5 is a diagram showing the relationship between the chamber flow rate and the oxygen concentration in the accommodation space 9.
  • the horizontal axis indicates the chamber flow rate
  • the vertical axis indicates the oxygen concentration in the accommodation space 9.
  • the oxygen concentration measurement results shown in Fig. 5 are measured when the curtain flow rate is 100 L / min.
  • the chamber flow rate is 100 L / min or more
  • the oxygen concentration in the accommodation space 9 can be kept below about 70 ppm, which indicates that the exhaust effect by the inert gas supplied from the gas supply means 15 appears remarkably.
  • the chamber flow rate is 300 L / min or more
  • the oxygen concentration in the accommodation space 9 can be kept at about 10 ppm or less, and the exhaust effect by the inert gas supplied from the gas supply means 15 is particularly noticeable. Is shown. Therefore, in the substrate manufacturing apparatus 1 of the present embodiment, the chamber flow rate is selected to be 100 L / min or more, preferably 300 L / min or more.
  • each buffer chamber 6 has one communication hole 17 and the size thereof is 400 mm ⁇ 100 mm.
  • the Reynolds number Re hereinafter referred to as “Channo Reynolds”.
  • the Reno's number Re is 734 when the chamber flow rate is 200 L / min
  • the Channo Reynolds number Re is 550 when the chamber flow rate is 150 L / min.
  • the Cyanno Reynolds number Re is 367.
  • the chamber 'Reikarezu number Re is selected to be 367 or more, and preferably 1100 or more.
  • the curtains 'Reynolds number Re and Channo' Reynolds number Re to achieve this oxygen concentration are based on Figs. 4 and 5, respectively. Determined.
  • equation (1) from the curtain 'Reikarezu number Re and chamber Reikarezu number Re, from the newly designed substrate manufacturing equipment 1 from the representative flow velocity U of the inert gas flowing from the gas ejection holes and from the accommodation space 9
  • the typical flow rate U of the inert gas passing through the communication hole 17 can be calculated, and the curtain flow rate and the chamber flow rate can be estimated by multiplying the flow rate by the opening area.
  • the curtain flow rate and the chamber flow rate can be estimated in advance at the time of design, and the design can be made in consideration of the amount of inert gas used and the oxygen concentration of the storage space 9.
  • the inert gas supplied to the accommodation space 9 by the gas supply means 15 flows into the buffer space 25 through the communication hole 17 and passes through the exhaust hole 34. It is exhausted from the buffer space 25 through. Therefore, even if a gas such as oxygen flows into the storage space 9, the gas flowing in along this inert gas flow is stored.
  • the space 9 and the buffer space 25 can be evacuated, and the containing space 9 can be filled with an inert gas.
  • the shirt 33 opens the transport hole 23 when the base plate 4 passes through the transport hole 23, and closes the transport hole 23 when the base plate 4 does not pass through the transport hole 23. Accordingly, it is possible to prevent the outside air such as air from flowing into the buffer space 25 when the base plate 4 does not pass through the transport hole 23. Even if outside air such as air flows into the buffer space 25 when the transfer hole 23 is open, the inflowing gas flows along with the flow of inert gas flowing from the storage space 9 through the buffer space 25 to the exhaust hole. Since the air is exhausted from the exhaust hole 34, it is possible to prevent the outside air from flowing into the housing space 9.
  • the gas ejection means 35 ejects an inert gas toward the base plate 4 conveyed in the buffer space 25.
  • an inert gas onto the base plate 4, it moves with the base plate 4 carried into the buffer space 25 from the outside of the substrate manufacturing apparatus 1, and gas such as oxygen covering the base plate 4 is separated from the base plate 4. Can do.
  • the gas thus separated from the base plate 4 is exhausted from the exhaust hole 34 together with the flow of the inert gas flowing from the storage space 9 through the buffer space 25 to the exhaust hole 34, so that the base plate 4 is stored in the storage space. It is possible to prevent outside air or the like from flowing into the accommodation space 9 when transported to the housing 9.
  • the storage space 9 can be filled with an inert gas, and the oxygen concentration is reduced!
  • the substrate can be manufactured in an inert gas atmosphere kept at a minimum. This prevents impurities from being mixed into the substrate 12 when the melt 11 is solidified and grown.
  • the oxygen concentration in the storage space 9 can be reduced to a low value by preventing the outside air from flowing into the storage space 9, a device provided in the storage space 9 such as the crucible 2 that is hot.
  • the chamber can be prevented from being oxidized and consumed, and the life of the substrate manufacturing apparatus 1 can be extended.
  • the crucible 2 and the transporting means 5 are formed to contain carbon, so that the crucible 2 and the transporting means 5 are oxidized and consumed by suppressing the oxygen concentration in the accommodation space 9 to a low value. Can be prevented. Since the oxygen concentration in the housing space 9 can be suppressed to a low value with a simple configuration that does not include an apparatus for a vacuum environment like the substrate manufacturing apparatus 101 of the prior art, the substrate manufacturing apparatus 1 can be downsized. The installation area is reduced and the cost is low. The board manufacturing apparatus 1 can be realized.
  • the gas jetting means 35 is provided on the lower wall 36 of the lower Z2 of the buffer chamber body 19 and jets an inert gas to the upper Z1. As long as the inert gas is ejected toward the exhaust hole 34, it may be disposed at any position.
  • FIG. 6 is a cross-sectional view of the buffer chamber 6 when the gas ejection means 35 is provided on the one side wall 39 in the first direction X of the buffer chamber body 19.
  • the connecting pipe 22 is connected from the other side wall 40 in the first direction X to the other side in the first direction X of the buffer chamber body 19. It is formed to extend.
  • the gas ejection means 35 ejects an inert gas to the other side in the first direction X toward the exhaust pipe 8.
  • the gas ejection means 35 is provided at the end of the one side wall 39 of the buffer chamber body 19 near the transfer pipe 21 in the first direction X.
  • the gas ejection means 35 extends along the one side wall 39 between both end portions in the vertical direction Z of the one side wall 39. At the other end portion in the first direction of the gas ejection means 35, an ejection hole extending between both end portions in the vertical direction Z is formed.
  • the gas ejection means 35 ejects an inert gas from the ejection hole toward the other side in the first direction X.
  • the ejection hole of the gas ejection means 35 is a long hole that is long in the extending direction (vertical direction Z) of the gas ejection means 35, and the inner peripheral surface facing the ejection hole has a rectangular cylindrical shape.
  • FIG. 6 the flow of the inert gas ejected from the gas ejection holes is indicated by arrows 41.
  • the opening 37 force S is formed on the other side wall 30 in the second direction Y of the buffer chamber body 19 by the transfer hole 23.
  • the opening 37 extends in the first direction X, and is formed in the other of the gas ejection means 35 in the first direction X as viewed from one of the second directions Y.
  • the opening 37 is formed at the center of the gas ejection hole in the vertical direction Z.
  • the width dimension W3 in the extending direction of the gas ejection hole (hereinafter referred to as the dimension W3 in the longitudinal direction of the gas ejection hole) is the width dimension in the extending direction of the gas ejection means 35 of the opening 37 formed in the other side wall 30.
  • W4 width dimension W4 of the opening 37
  • W4 width dimension W4 of the opening 37
  • W4 of the opening 37 width dimension W4 of the opening 37
  • the shape of the gas ejection hole in this way, as described above, the area surrounded by the virtual plane extending the surface defining the transport hole 23, that is, the inner peripheral surface of the transport pipe 21 facing the transport hole 23 (FIG. 6). In the area in the opening 37) In this case, the flow of the inert gas is not disturbed, and the outside air flowing from the transfer hole 23 can be effectively exhausted to the exhaust hole 34. As a result, the outside air can be prevented from flowing into the accommodation space 9 through the communication hole 17 and the oxygen concentration in the accommodation space 9 can be reduced.
  • the inert gas is generated from the direction parallel to the surface 4a of the base plate 4 on which the substrate 12 is formed, that is, from the direction perpendicular to the surface of the plate-like base plate 4 having a small area. Will be injected. For this reason, the inert gas is sprayed evenly on the surface 4a of the base plate 4 on which the substrate 12 is formed and the surface facing the surface 4a, and the outside air conveyed over the surface facing the surface 4a. Can be quickly and reliably eliminated. Furthermore, disturbance of the inert gas flow by the base plate 4 is unlikely to occur.
  • the chamber 3 and the buffer chamber 6 are formed symmetrically with respect to the second axis L2, but may not be symmetrical.
  • the gas supply means 15 adjusts the flow rate of the inert gas flowing from each inert gas inflow hole 16, thereby passing through the communication hole 17 of each buffer chamber 6 to each buffer space 25.
  • the inert gas is supplied to the accommodating space 9 so that the flow rate of the inert gas flowing in is equal. As a result, it is possible to prevent outside air from flowing into the accommodation space 9 from the buffer space 25 as described above, and to reduce the oxygen concentration in the accommodation space 9.
  • FIG. 7 is a cross-sectional view of the buffer chamber 6 of the substrate manufacturing apparatus 1 according to another embodiment of the present invention.
  • the substrate manufacturing apparatus 1 according to the present embodiment has the same configuration except for the structure of the substrate manufacturing apparatus 1 and the buffer chamber 6 according to the above-described embodiment. Are denoted by the same reference numerals, and redundant description is omitted.
  • the communication pipe 20 extends in a tapered shape from the end of the buffer chamber body 19 near the chamber 3 toward the chamber 3. Therefore, the communication hole 17 is also formed in a tapered shape as it approaches the accommodating space 9 from the buffer space 25. In other words, the opening area of the communication pipe 20 is formed so as to decrease as it approaches the accommodation space 9 from the buffer space 25.
  • connection pipe 22 is formed so that a cross section perpendicular to the vertical direction Z increases as the distance from the upper wall 31 of the buffer chamber body 19 increases to the upper Z1. Therefore, the area of the cross section of the exhaust hole 34 perpendicular to the up-down direction Z, that is, the opening area of the connection pipe 22 is formed so as to increase as the distance from the buffer chamber body 19 to the upper side Z1 increases.
  • the transport pipe 21 is formed so that a cross section perpendicular to the extending direction of the transport pipe 21 increases as the distance from the other side wall 30 of the buffer chamber body 19 to the side opposite to the chamber 3 increases. Therefore, the area of the cross section of the transport hole 23 perpendicular to the direction in which the transport pipe 21 extends, that is, the opening area of the transport pipe 21 is formed to increase as the distance from the buffer chamber body 19 increases.
  • the resistance due to the gas flow path is inversely proportional to the inner diameter and proportional to the square of the flow velocity. Accordingly, in the case of a channel having a tapered shape, the inner diameter is reduced and the flow velocity is increased as the cross-sectional area of the channel is reduced, so that the resistance by the channel is increased. That is, gas flows more easily in the direction in which the cross-sectional area of the flow path becomes larger than in the direction in which the cross-sectional area of the flow path decreases. Since the communication pipe 20 has the tapered shape described above, gas flows from the storage space 9 through the communication pipe 20 to the buffer space 25 rather than from the buffer space 25 through the communication hole 17 to the storage space 9. easy. As a result, it is possible to prevent outside air from flowing into the accommodation space 9 from the buffer chamber main body 19, and to maintain the oxygen concentration in the accommodation space 9 at a low value.
  • the connecting pipe 22 has the tapered shape described above, it is difficult for gas to flow into the buffer space 25 from the pipe line formed by the exhaust pipe 8, and gas containing oxygen or the like exhausted from the nother space 25 is buffered. Can prevent backflow.
  • the transfer pipe 21 has the above-described tapered shape, it is difficult for outside air to flow into the buffer space 25 through the transfer hole 23. By these, the oxygen concentration in the buffer space 25 can be kept at a low value, and as a result, the oxygen concentration in the accommodation space 9 can be kept at a low value. As a result, it is possible to prevent impurities from being mixed into the substrate 12 as described above, and to extend the life of the substrate manufacturing apparatus 1.
  • FIG. 8 is a sectional view showing a substrate manufacturing apparatus 51 according to still another embodiment of the present invention.
  • the substrate manufacturing apparatus 51 of the present embodiment further includes a replenishing means 52 that replenishes the raw material 69 of the substrate 12 in addition to the substrate manufacturing apparatus 1 of each of the above-described embodiments.
  • the substrate manufacturing apparatus 51 of the present embodiment has a configuration in which the replenishing means 52 is added to the substrate manufacturing apparatus 1 of each of the above-described embodiments. Only the explanation is omitted, and the duplicate explanation is omitted. In Fig. 8, for ease of understanding, The step 5, the base plate 4, the transfer means 7 and the gas supply means 15 are omitted.
  • the replenishing means 52 supplies the crucible 2 with a raw material 69 such as a solid or liquid metal material and a semiconductor material in order to supplement the reduced amount of the raw material 69.
  • the replenishing means 52 supplies the solid raw material 69 to the crucible 2.
  • the replenishing means 52 passes through the replenishment buffer chamber 53 provided in the upper Z1 of the chamber 3 and the opening formed in the upper wall 54 of the upper Z1 of the chamber 3 from the replenishing buffer chamber 53 to the accommodation space 9.
  • an opening / closing means provided with a shirt capable of opening and closing a formed pipe line (hereinafter referred to as a replenishment conveying hole) 65.
  • the shirter 66 opens the supply transport hole 65 when the raw material 69 is supplied to the crucible 2, and closes the supply transport hole 65 at other times.
  • the replenishment transport hole 65 is opened, the raw material 69 is supplied to the buffer space 68 formed by the replenishment buffer chamber 53, and further passes through the conduit 70 formed by the replenishment pipe 55, and the crucible 2 To be supplied.
  • the gas ejection means 64 is connected to the gas ejection means 64 and the connection pipe by ejecting an inert gas toward the pipe line 71 formed by the connection pipe 63, in the same manner as the gas ejection means 35 of each of the foregoing embodiments. Inert gas is spouted toward the raw material 69 that passes between them. As described above, the gas ejection means 64 ejects the inert gas, so that the outside air can be prevented from flowing into the accommodation space 9, and the oxygen concentration in the accommodation space 9 can be kept at a low value. it can. As a result, it is possible to prevent impurities from being mixed into the substrate 12 as described above, and to further extend the life of the substrate manufacturing apparatus 1.
  • the substrate manufacturing apparatus 51 further includes a recovery unit that recovers fragments of the substrate 12.
  • a recovery unit that recovers fragments of the substrate 12.
  • the substrate 12 formed on one surface 4a of the base plate 4 is separated from the melt 11, the substrate 12 suddenly changes from a high temperature to a low temperature. Because it is cooled extremely, thermal stress is generated and it breaks, and there is a possibility that debris falls on the lower wall of Z2 below chamber 3.
  • the collecting means collects the broken pieces of the substrate 12 that have dropped on the lower wall of the chamber for reuse.
  • the collecting means includes a tray disposed at a position where the fragments of the substrate 12 are highly likely to fall, and a transport unit that carries the trays accommodating the fragments of the substrate 12 out of the accommodation space 9.
  • the chamber 3 is formed with an opening through which the recovery means passes, and the buffer chamber 6 having the same configuration as the buffer chamber 6 of each of the above-described embodiments is connected to the opening forming the opening. Further, in the buffer space 25, the gas jetting means 35 and the opening / closing means 24 are provided as in the above-described embodiments.
  • the inert gas ejected from the gas ejection means 35 forms a barrier that blocks the outside air from flowing from the transport hole 23 through the buffer space 25 and the communication hole 17 into the accommodation space 9. This prevents the outside air from flowing into the storage space 9 when the tray is carried into or out of the buffer chamber 6, and the oxygen concentration in the storage space 9 can be kept at a low level. it can.
  • the inert gas is supplied to the accommodation space by the gas supply means.
  • the inert gas supplied to the storage space flows into the buffer space through the communication hole, and is exhausted from the buffer space through the exhaust hole. Therefore, even if a gas such as oxygen flows into the accommodation space, the gas flowing along the flow of the inert gas can be exhausted from the accommodation space and the buffer space, and the accommodation space is filled with the inert gas.
  • the opening / closing means includes a shirter capable of opening and closing the transport hole. For example, this shatter opens the transport hole when the cooling body passes through the transport hole, and does not pass through the transport hole. Close the transport hole.
  • the gas jetting means jets an inert gas toward the cooling body conveyed in the buffer space.
  • the gas moves together with the cooling body carried into the buffer space from the outside of the substrate manufacturing apparatus, and the gas such as oxygen covering the cooling body can be separated from the cooling body.
  • the gas thus separated from the cooling body is exhausted together with the flow of the inert gas flowing from the accommodation space through the buffer space to the exhaust hole, so that when the cooling body is transported to the accommodation space, the outside air or the like is exhausted. Can prevent the flow of water into the containment space.
  • the storage space can be filled with an inert gas, and the oxygen concentration is suppressed to a low value.
  • the substrate can be manufactured in an active gas atmosphere. As a result, it is possible to prevent impurities from entering the substrate when the melt is solidified and grown.
  • the outside air can be prevented from flowing into the storage space and the oxygen concentration in the storage space can be kept to a low value, the equipment provided in the chamber such as the crucible and the chamber and the chamber are oxidized and consumed. The ability to extend the life of substrate manufacturing equipment can be prevented.
  • since there is no need to provide a device for a vacuum environment it is possible to prevent the substrate manufacturing apparatus from becoming complicated and large in size and to increase the installation area, and to reduce the cost of the substrate manufacturing apparatus.
  • the inert gas having the same flow rate flows through the communication hole of each buffer chamber by the gas supply means. If the flow rate of the inert gas flowing through one or more specific communication holes of the plurality of communication holes is small! /, If the flow rate is low, the force that allows outside air to easily flow into the accommodation space from the communication holes. Then, since the flow rate of the inert gas flowing through each communication hole is equal, it is possible to prevent the outside air from flowing into the accommodation space. As a result, the oxygen concentration in the accommodation space can be reduced, impurities can be prevented from being mixed into the substrate as described above, and the life of the substrate manufacturing apparatus can be extended.
  • the volume of the buffer chamber is selected to be more than 0% and not more than 10% of the chamber volume. Since the inert gas supplied from the gas supply means flows into the buffer space from the storage space, the pressure in the buffer space is at least higher than atmospheric pressure. If the pressure in the buffer space is higher than atmospheric pressure, it is possible to prevent outside air from flowing into the buffer space when the transfer hole is open.
  • the volume of the buffer chamber is larger than 10% of the volume of the chamber, the effect of increasing the pressure in the buffer space decreases, so the difference between the atmospheric pressure and the pressure in the buffer space decreases, and the outside air flows into the buffer space. The effect of preventing the inflow is reduced.
  • the gas jetting means is provided close to the transport hole in the buffer space. That is, the gas jetting means jets an inert gas to the cooling body near the transport hole in the buffer space near the communication hole.
  • the gas such as oxygen covering the cooling body is separated at a position away from the transport hole in this way, it is possible to prevent the separated gas from passing through the transport hole as much as possible, and to prevent outside air from flowing into the accommodation space. it can.
  • the oxygen concentration in the housing space can be reduced, as described above, impurities can be prevented from being mixed into the substrate, and the life of the substrate manufacturing apparatus can be extended.
  • the opening / closing means is provided close to the transport hole, the gap between the opening / closing means and the transport hole is narrowed. Therefore, it is possible to prevent gas such as air from flowing into the accommodation space from this gap. As a result, the oxygen concentration in the housing space can be reduced, impurities can be prevented from being mixed into the substrate as described above, and the life of the substrate manufacturing apparatus can be extended.
  • the gas ejection means ejects the inert gas toward the exhaust hole, a flow of inert gas from the gas ejection means to the exhaust hole occurs.
  • gas such as oxygen separated from the cooling body
  • gas such as oxygen separated from the cooling body
  • oxygen away from the cooling body It is possible to prevent any gas from flowing into the accommodation space through the communication hole.
  • the oxygen concentration in the accommodation space can be reduced, as described above, impurities can be prevented from being mixed into the substrate, and the life of the substrate manufacturing apparatus can be extended.
  • the gas jetting means jets gas over the outside of the region into a region surrounded by a virtual surface extending the surface defining the transport hole. Since the gas is ejected to the outside of the region, the gas flow is not disturbed at the end of the region in the direction perpendicular to the direction in which the gas is ejected, and the outside air flowing from the transfer hole is more effectively exhausted.
  • the holes can be evacuated. As a result, it is possible to reduce the oxygen concentration in the accommodation space by preventing outside air from flowing into the accommodation space through the communication hole, and to prevent impurities from being mixed into the substrate as described above. Use S to extend the life of the board manufacturing equipment.
  • the gas ejection means is formed to extend in a predetermined direction perpendicular to the direction in which the gas is ejected, and has an ejection hole through which the gas is ejected, and in the direction in which the gas is ejected and the predetermined direction.
  • the width dimension of the jet hole in the vertical direction is selected to be not less than 0.05 mm and less than 0.2 mm.
  • the inert gas ejected from the gas ejection means is selected as at least one of a rare gas and a nitrogen gas. Since the gas ejection means ejects such an inert gas, even if the inert gas ejected from the gas ejection means flows into the accommodation space through the communication hole, impurities are not mixed into the substrate. Further, the apparatus provided in the chamber such as a crucible at a high temperature and the chamber do not react with the inert gas ejected from the gas ejection means and are not consumed. As a result, as described above, impurities can be prevented from being mixed into the substrate, and the life of the substrate manufacturing apparatus can be extended.
  • the gas ejection means ejects the inert gas in a direction parallel to the surface of the cooling body for solidifying and growing the raw material. Therefore, even when the cooling body is plate-shaped and the substrate is formed on the surface having the largest surface area, the cooling body hardly disturbs the flow of the inert gas. Also, the surface that forms the substrate and the surface that faces this surface Inert gas is sprayed evenly Thus, the outside air that is transported covering both surfaces is quickly and reliably eliminated.

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Abstract

Substrate production equipment in which oxygen concentration in a chamber can be reduced through a simple arrangement. A crucible (2) for storing a melt (11) produced by thermally melting the material of a substrate (12) is provided in a containing space (9) formed by a chamber (3). A buffer chamber (6) forming a buffer space (25) communicates with the containing space (9), and is connected with a communication hole (17) which can pass a cooling body, an exhaust hole (34) for exhausting a gas, and the outer space, and provided with a conveyance hole (23) which can pass the cooling body. The buffer space (25) communicates with the communication hole (17), the exhaust hole (34) and the conveyance hole (23). The conveyance hole (23) can be opened/closed by means of a shutter (33) of an opening/closing means (24), and it is opened when an underlying plate (4) passes. The containing space (9) is supplied with an inert gas by a gas supply means (15). A gas jet means (35) jets the inert gas toward the cooling body when a conveyance means (7) conveys the underlying plate (4) in the buffer space (25).

Description

明 細 書  Specification

基板製造装置  Board manufacturing equipment

技術分野  Technical field

[0001] 本発明は、金属または半導体の融液から薄板状の基板を製造する基板製造装置 に関する。  The present invention relates to a substrate manufacturing apparatus for manufacturing a thin plate substrate from a metal or semiconductor melt.

背景技術  Background art

[0002] 薄板状の基板を製造する方法として、結晶リボン法および EFG (Edge-defined Film -fed Growth)法が知られている。これらの方法を実現する基板製造装置は、結晶成 長が行われるチャンバ外に駆動部が設けられるので、装置が小形になると!/、う利点 がある(たとえば特開 2001— 322892号公報参照)。し力、しこれらの方法では、基板 の厚み方向に結晶成長を行うのではなぐ基板の厚み方向に垂直な向きに結晶成 長を行って基板を製造して!/、るので、基板の生産性が低!/、と!/、う問題がある。  [0002] As a method of manufacturing a thin plate-like substrate, a crystal ribbon method and an EFG (Edge-defined Film-fed Growth) method are known. The substrate manufacturing apparatus that realizes these methods has a drive unit provided outside the chamber in which crystal growth is performed, so there is an advantage that the apparatus becomes small! (See, for example, JP-A-2001-322892) . In these methods, the substrate is produced by crystal growth in a direction perpendicular to the thickness direction of the substrate rather than crystal growth in the thickness direction of the substrate! / The problem is low! /, And! /

図 9は、他の従来の技術の基板製造装置 101を示す断面図である。基板製造装置 101では、基板の材料の融液 102に板状の冷却体 103を浸漬させ、冷却体 103の 厚み方向の表面 103a上に融液 102を結晶成長させて基板を製造している。これに よって基板の生産性を高くしている。  FIG. 9 is a cross-sectional view showing another conventional substrate manufacturing apparatus 101. The substrate manufacturing apparatus 101 manufactures a substrate by immersing a plate-like cooling body 103 in a melt 102 of the substrate material and crystal-growing the melt 102 on the surface 103 a in the thickness direction of the cooling body 103. This increases the productivity of the substrate.

基板製造装置 101は、融液 102を収容する坩堝 111と、冷却体 103を保持して融 液 102に浸漬する運搬手段 104と、坩堝 111および運搬手段 104を収容するチャン ノ 105と、ロードロック室 106と、ゲートバルブ 107と、真空ポンプ 108とを含んで構成 される。図 9において運搬手段 104の動く向きを矢符 109で示す。  The substrate manufacturing apparatus 101 includes a crucible 111 that accommodates the melt 102, a transport means 104 that holds the cooling body 103 and is immersed in the melt 102, a channel 105 that houses the crucible 111 and the transport means 104, and a load lock. The chamber 106 is configured to include a gate valve 107 and a vacuum pump 108. In FIG. 9, the moving direction of the conveying means 104 is indicated by an arrow 109.

ロードロック室 106は、チャンバ 105内に冷却体 103を搬入するときに通過する搬 入用のロードロック室(図 9において左側に位置する)と、チャンバ 105内から基板製 造装置 101外に冷却体 103を搬出するときに冷却体 103が通過する搬出用のロード ロック室(図 9において右側に位置する)とを含んで構成される。搬入用および搬出用 のロードロック室 106は、それぞれゲートバルブ 107によってチャンバ 105と仕切られ るとともに、外気からも遮蔽される。ゲートバルブ 107は、冷却体 103が通過するとき にのみ開状態になる。チャンバ 105内と、搬入用および搬出用のロードロック室 106 内とは、真空ポンプ 108によってそれぞれ真空引きされるとともに、チャンバ 105内に は不活性ガスが供給される。図 9において不活性ガスの流れる向きを矢符 110で示 す。このようにロードロック方式を用いることで、チャンバ 105内に外気が流入すること を防いで、チャンバ 105内を不活性ガスの雰囲気に保つことができる。 The load lock chamber 106 is a load lock chamber for loading (positioned on the left side in FIG. 9) that passes when the cooling body 103 is loaded into the chamber 105, and is cooled outside the substrate manufacturing apparatus 101 from within the chamber 105. And a load lock chamber (located on the right side in FIG. 9) through which the cooling body 103 passes when the body 103 is unloaded. The load lock chamber 106 for loading and unloading is separated from the chamber 105 by a gate valve 107, and is also shielded from outside air. The gate valve 107 is opened only when the cooling body 103 passes. Inside the chamber 105 and the load lock chamber 106 for loading and unloading The inside is evacuated by a vacuum pump 108 and an inert gas is supplied into the chamber 105. In FIG. 9, the flow direction of the inert gas is indicated by an arrow 110. By using the load lock method in this way, it is possible to prevent the outside air from flowing into the chamber 105 and keep the inside of the chamber 105 in an inert gas atmosphere.

このような基板製造装置 101では、チャンバ 105内において冷却体 103を予め定 める経路および速度で搬送する運搬手段 104などの駆動部をチャンバ 105内に備 える必要が生じ、チャンバが大形化してしまうが、冷却体 103の表面から基板の厚み 方向に基板を成長させることができるので、基板の製造速度を上げることができる。こ のようにして、基板の生産性の高い基板製造装置を実現している(たとえば特開 200 4 161583号公報参照)。  In such a substrate manufacturing apparatus 101, it becomes necessary to provide a driving unit such as a conveying means 104 for transporting the cooling body 103 at a predetermined path and speed in the chamber 105, and the chamber becomes larger. However, since the substrate can be grown in the thickness direction of the substrate from the surface of the cooling body 103, the manufacturing speed of the substrate can be increased. In this way, a substrate manufacturing apparatus with high substrate productivity is realized (see, for example, Japanese Patent Application Laid-Open No. 2004 161583).

チャンバ 105内において化学的に活性の高い酸素などの濃度が高くなると、基板 の材料となる融液 102に不純物が混入して、純度および結晶性などの点において質 の高い基板を製造することができない。そこで前述した従来の基板製造装置 101で は、チャンバ 105内を真空にするとともに、不活性ガスをチャンバ 105内に供給する ことによって酸素などを排除している力 チャンバ 105内を真空に保っために、ロード ロック室 106、ゲートバルブ 107および真空ポンプ 108などの真空環境用の装置が 必要となる。このように真空環境用の装置が必要となるので、基板製造装置 101が複 雑化および大形化して設置面積が大きくなり、基板製造装置 101のコストが高くなる という問題が生じる。  When the concentration of chemically active oxygen or the like increases in the chamber 105, impurities are mixed into the melt 102, which is a material of the substrate, and a substrate having a high quality in terms of purity and crystallinity can be manufactured. Can not. Therefore, in the conventional substrate manufacturing apparatus 101 described above, the inside of the chamber 105 is evacuated, and an inert gas is supplied into the chamber 105 to eliminate oxygen and the like. Equipment for vacuum environment such as load lock chamber 106, gate valve 107 and vacuum pump 108 is required. Since an apparatus for a vacuum environment is required in this way, there arises a problem that the substrate manufacturing apparatus 101 is complicated and enlarged, the installation area is increased, and the cost of the substrate manufacturing apparatus 101 is increased.

また金属材料または半導体材料の融液 102を収容する坩堝 111は、坩堝 111を形 成する材料が融液 102に混交するコンタミネーシヨンを防ぐために、石英ガラスまた はカーボンを用いて形成される。特に使い捨て用の坩堝 111の場合には、石英ガラ スよりもカーボンの方がコストが低いので、カーボンを用いて形成されることが多い。 またチャンバ 105内に設けられる運搬手段 104などの駆動装置も同様の理由から力 一ボンを用いて形成されることが多レ、。  In addition, the crucible 111 containing the melt 102 of the metal material or the semiconductor material is formed using quartz glass or carbon in order to prevent contamination of the material forming the crucible 111 with the melt 102. In particular, in the case of the disposable crucible 111, since carbon is lower in cost than quartz glass, it is often formed using carbon. Also, for the same reason, drive devices such as the transport means 104 provided in the chamber 105 are often formed using a single bonnet.

カーボンは、酸素雰囲気において 400°C以上の高温になると酸化して気体の二酸 化炭素に変化するので (化学反応式: C + O→CO )、チャンバ 105内の酸素の濃  Since carbon oxidizes and changes to gaseous carbon dioxide when it reaches a high temperature of 400 ° C or higher in an oxygen atmosphere (chemical reaction formula: C + O → CO), the concentration of oxygen in the chamber 105

2 2  twenty two

度が高くなると、カーボンによって形成される坩堝 111および駆動装置が消耗してし まうという問題がある。そこで従来の基板製造装置 101では、チャンバ 105内の酸素 の濃度を低くするために、真空環境用の装置を用いてチャンバ 105内の酸素などを 排除しているが、前述した問題と同様に基板製造装置 101が複雑化および大形化し て設置面積が大きくなり、基板製造装置 101のコストが高くなるという問題が生じる。 発明の開示 As the temperature increases, the crucible 111 formed of carbon and the driving device are worn out. There is a problem. Therefore, in the conventional substrate manufacturing apparatus 101, in order to reduce the concentration of oxygen in the chamber 105, oxygen in the chamber 105 is excluded by using a vacuum environment apparatus. The manufacturing apparatus 101 becomes complicated and large, so that the installation area increases, and the cost of the board manufacturing apparatus 101 increases. Disclosure of the invention

したがって本発明の目的は、簡易な構成でチャンバ内の酸素濃度を低減すること ができる基板製造装置を提供することである。  Accordingly, an object of the present invention is to provide a substrate manufacturing apparatus capable of reducing the oxygen concentration in a chamber with a simple configuration.

本発明は、基板の原料を加熱溶融した融液に冷却体を浸漬し、前記冷却体の表 面上に前記原料を凝固成長させて基板を製造する基板製造装置であって、 前記融液を貯留する坩堝を備え、前記坩堝が収容される収容空間を形成するチヤ ンバと、  The present invention is a substrate manufacturing apparatus for manufacturing a substrate by immersing a cooling body in a melt obtained by heating and melting a raw material of a substrate, and solidifying and growing the raw material on a surface of the cooling body. A chamber that includes a crucible for storage, and that forms a storage space in which the crucible is stored;

前記収容空間に不活性ガスを供給するガス供給手段と、  Gas supply means for supplying an inert gas to the accommodation space;

前記収容空間に連通し、かつ冷却体が通過可能な連通孔、ガスが排気される排気 孔、および外部空間に連なり、かつ冷却体が通過可能な搬送孔が形成され、前記連 通孔、排気孔および搬送孔に連通するバッファ空間を形成するバッファ室と、 前記搬送孔を開閉可能なシャツタを備える開閉手段と、  A communication hole that communicates with the housing space and allows the cooling body to pass therethrough, an exhaust hole that exhausts gas, and a transport hole that communicates with the external space and allows the cooling body to pass therethrough are formed. A buffer chamber that forms a buffer space communicating with the hole and the transport hole; and an opening / closing means that includes a shirter capable of opening and closing the transport hole;

前記連通孔および搬送孔を通って、収容空間に冷却体を搬入し、かつ収容空間か ら冷却体を搬出する搬送手段と、  A conveying means for carrying the cooling body into the accommodation space through the communication hole and the conveyance hole and carrying out the cooling body from the accommodation space;

バッファ空間に収容され、搬送手段によってバッファ空間を搬送される冷却体に向 けて不活性ガスを噴出するガス噴出手段とを含むことを特徴とする基板製造装置で ある。  A substrate manufacturing apparatus including gas ejection means for ejecting an inert gas toward a cooling body accommodated in the buffer space and conveyed through the buffer space by the conveyance means.

また本発明は、複数の前記バッファ室を有し、  The present invention also includes a plurality of the buffer chambers,

前記ガス供給手段は、各バッファ室の連通孔を通って各バッファ空間にそれぞれ 流入する不活性ガスの流量が等しくなるように前記収容空間に不活性ガスを供給す ることを特徴とする。  The gas supply means supplies the inert gas to the accommodation space so that the flow rates of the inert gas flowing into the buffer spaces through the communication holes of the buffer chambers become equal.

また本発明は、前記バッファ室の容積は、前記チャンバの容積の 0%を超えてかつ 10%以下に選ばれることを特徴とする。  In the invention, it is preferable that the volume of the buffer chamber is selected to be more than 0% and 10% or less of the volume of the chamber.

また本発明は、前記ガス噴出手段は、バッファ空間で搬送孔寄りに近接して設けら れることを特徴とする。 Further, according to the present invention, the gas ejection means is provided in the buffer space close to the transport hole. It is characterized by that.

また本発明は、前記開閉手段は、前記搬送孔に近接して設けられることを特徴とす また本発明は、前記ガス噴出手段は、排気孔に向けて不活性ガスを噴出することを 特徴とする。  Further, the present invention is characterized in that the opening / closing means is provided in the vicinity of the transport hole. Also, the invention is characterized in that the gas ejection means ejects an inert gas toward the exhaust hole. To do.

また本発明は、前記ガス噴出手段は、前記搬送孔を規定する面を延長した仮想面 によって囲まれる領域に、前記領域の外方にわたってガスを噴出することを特徴とす また本発明は、前記ガス噴出手段は、不活性ガスが噴出する方向に垂直な予め定 める方向に延びて形成され、不活性ガスが噴出する噴出孔を有し、  Further, the present invention is characterized in that the gas jetting means jets gas over the outside of the region into a region surrounded by a virtual surface extending the surface defining the transport hole. The gas ejection means is formed to extend in a predetermined direction perpendicular to the direction in which the inert gas is ejected, and has an ejection hole through which the inert gas is ejected.

ガスが噴出する方向および前記予め定める方向に垂直な方向の前記噴出孔の幅 の寸法は、 0. 05mm以上かつ 0. 2mm未満に選ばれることを特徴とする。  The width dimension of the ejection hole in the gas ejection direction and the direction perpendicular to the predetermined direction is selected to be 0.05 mm or more and less than 0.2 mm.

また本発明は、前記ガス噴出手段は、原料を凝固成長させる冷却体の表面に対し て平行な方向に、不活性ガスを噴出することを特徴とする。  Further, the present invention is characterized in that the gas jetting means jets an inert gas in a direction parallel to a surface of a cooling body for solidifying and growing the raw material.

また本発明は、前記ガス噴出手段から噴出される不活性ガスは、希ガスおよび窒素 ガスのうちの少なくともいずれか一方に選ばれることを特徴とする。  The present invention is characterized in that the inert gas ejected from the gas ejection means is selected from at least one of a rare gas and a nitrogen gas.

図面の簡単な説明 Brief Description of Drawings

本発明の目的、特色、および利点は、下記の詳細な説明と図面とからより明確にな るであろう。  Objects, features and advantages of the present invention will become more apparent from the following detailed description and drawings.

図 1は、本発明の実施の一形態の基板製造装置 1の構成を模式的に示す断面図 である。  FIG. 1 is a cross-sectional view schematically showing a configuration of a substrate manufacturing apparatus 1 according to an embodiment of the present invention.

図 2は、図 1のセクション IIの拡大断面図である。  FIG. 2 is an enlarged cross-sectional view of section II of FIG.

図 3は、図 2の切断面線 III— IIIから見たバッファ室 6の断面図である。  FIG. 3 is a cross-sectional view of the buffer chamber 6 as seen from the section line III-III in FIG.

図 4は、ガス噴出手段 35から噴出される不活性ガスの流量と、収容空間 9の酸素 濃度との関係を示す図である。  FIG. 4 is a diagram showing the relationship between the flow rate of the inert gas ejected from the gas ejection means 35 and the oxygen concentration in the accommodation space 9.

図 5は、チャンバ流量と、収容空間 9の酸素濃度との関係を示す図である。  FIG. 5 is a diagram showing the relationship between the chamber flow rate and the oxygen concentration in the accommodation space 9.

図 6は、ガス噴出手段 35をバッファ室本体 19の第 1方向 Xの一側壁 39に設けたと きのバッファ室 6の断面図である。 図 7は、本発明の他の実施の形態の基板製造装置 1のバッファ室 6の断面図であ 図 8は、本発明のさらに他の実施の形態の基板製造装置 51を示す断面図である 図 9は、他の従来の技術の基板製造装置 101を示す断面図である。 FIG. 6 is a cross-sectional view of the buffer chamber 6 when the gas ejection means 35 is provided on the one side wall 39 in the first direction X of the buffer chamber body 19. FIG. 7 is a cross-sectional view of a buffer chamber 6 of a substrate manufacturing apparatus 1 according to another embodiment of the present invention. FIG. 8 is a cross-sectional view illustrating a substrate manufacturing apparatus 51 according to still another embodiment of the present invention. FIG. 9 is a cross-sectional view showing another conventional substrate manufacturing apparatus 101.

発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION

以下図面を参考にして本発明の好適な実施形態を詳細に説明する。  Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings.

図 1は、本発明の実施の一形態の基板製造装置 1の構成を模式的に示す断面図 である。基板製造装置 1は、坩堝 2を備え、この坩堝 2が収容される収容空間 9を形成 するチャンバ 3と、収容空間 9において冷却体(以下、下地板ともいう) 4を保持して運 搬する運搬手段 5と、 1または複数のバッファ室 6と、冷却体 4を収容空間 9に搬送す る、または収容空間 9から外に搬送する搬送手段 7と、排気管 8とを含んで構成される 。基板製造装置 1は、板状の下地板 4を融液 11に浸漬させることによって、下地板 4 の厚み方向の一表面 4a上に融液 11を凝固成長させて基板 12を製造する。基板製 造装置 1を用いて、たとえば太陽電池に用いられる低コストの薄板状のシリコン基板 を製造する。  FIG. 1 is a cross-sectional view schematically showing a configuration of a substrate manufacturing apparatus 1 according to an embodiment of the present invention. A substrate manufacturing apparatus 1 includes a crucible 2 and carries a chamber 3 that forms a storage space 9 in which the crucible 2 is stored, and a cooling body (hereinafter also referred to as a base plate) 4 in the storage space 9. Conveying means 5, one or a plurality of buffer chambers 6, a conveying means 7 that conveys the cooling body 4 to the accommodating space 9, or conveys it out of the accommodating space 9, and an exhaust pipe 8. . The substrate manufacturing apparatus 1 immerses the plate-like base plate 4 in the melt 11 to solidify and grow the melt 11 on the one surface 4 a in the thickness direction of the base plate 4 to manufacture the substrate 12. The substrate manufacturing apparatus 1 is used to manufacture a low-cost thin-plate silicon substrate used for, for example, a solar cell.

チャンバ 3は、坩堝 2を外囲して設けられる加熱手段をさらに備える。加熱手段は、 抵抗加熱装置および誘導加熱装置などによって実現される。加熱手段は、坩堝 2に 充填された固体状の基板 12の原料を融点以上の高温に加熱することによって、基板 12の原料を溶融する。基板 12の原料は、たとえば金属材料および半導体材料から 成る。坩堝 2は、加熱手段によって溶融された液体状の融液 11を収容する。本実施 の形態では、坩堝 2は、カーボンを含んで形成される。  The chamber 3 further includes heating means provided so as to surround the crucible 2. The heating means is realized by a resistance heating device, an induction heating device, or the like. The heating means melts the raw material of the substrate 12 by heating the raw material of the solid substrate 12 filled in the crucible 2 to a high temperature equal to or higher than the melting point. The raw material of the substrate 12 is made of, for example, a metal material and a semiconductor material. The crucible 2 contains a liquid melt 11 melted by a heating means. In the present embodiment, crucible 2 is formed containing carbon.

運搬手段 5は、下地板 4を運搬して融液 11に浸漬する。運搬手段 5は、基板製造 装置 1の使用状態において、坩堝 2の鉛直方向 Zの一方(以下、上方 Z1という)に配 置される。以下、基板製造装置 1の使用状態に基づいて説明する。運搬手段 5は、収 容空間 9において鉛直方向 Zに垂直な予め定める第 1方向 Xに平行な第 1軸線 L1ま わりに回転可能に軸支される軸体 18と、軸体 18から第 1軸線 L1を中心とする半径方 向の外方に延びる複数のアーム 13とを備える。複数のアーム 13は、第 1軸線 L1を中 心とする周方向に予め定める間隔をあけてそれぞれ配置される。図 1では、一例とし て 3本のアーム 13を示している。各アーム 13の第 1軸線 L1を中心とする半径方向の 外方の端部は、下地板 4を保持する保持部 14を構成する。本実施の形態では、保持 部 14は、下地板 4と嵌合する形状を有する。具体的には、保持部 14には、第 1軸線 L1を中心とする周方向の両端部間にわたって凹溝が形成され、下地板 4の厚み方 向の他表面部には、厚み方向に垂直な方向に延びる凸溝が形成され、この凸溝と凹 溝とが嵌合する。凹溝の延びる方向に垂直な断面は、台形状であって、より長い下底 がより短い上底に対して軸体 18寄りに形成される。凸溝の延びる方向に垂直な断面 は、前記凹溝の断面よりもやや小さぐ上底よりも長い下底が厚み方向の他方の先端 に形成される。アーム 13は、下地板 4の凸溝と保持部 14の凹溝とが嵌り込むことによ つて、下地板 4を保持する。本実施の形態では、運搬手段 5は、カーボンを含んで構 成される。 The transport means 5 transports the base plate 4 and immerses it in the melt 11. The transporting means 5 is arranged on one side of the crucible 2 in the vertical direction Z (hereinafter referred to as the upper Z1) when the substrate manufacturing apparatus 1 is in use. Hereinafter, description will be given based on the usage state of the substrate manufacturing apparatus 1. The transport means 5 includes a shaft body 18 that is rotatably supported around a first axis L1 parallel to a predetermined first direction X perpendicular to the vertical direction Z in the storage space 9, and a shaft 18 to the first axis. And a plurality of arms 13 extending outward in the radial direction centered on L1. Multiple arms 13 are centered on the first axis L1. They are arranged at predetermined intervals in the circumferential direction as the center. In FIG. 1, three arms 13 are shown as an example. An outer end portion in the radial direction around the first axis L1 of each arm 13 constitutes a holding portion 14 that holds the base plate 4. In the present embodiment, the holding portion 14 has a shape that fits with the base plate 4. Specifically, the holding portion 14 is formed with a groove between both end portions in the circumferential direction centered on the first axis L1, and the other surface portion in the thickness direction of the base plate 4 is perpendicular to the thickness direction. A convex groove extending in any direction is formed, and the convex groove and the concave groove are fitted. The cross section perpendicular to the direction in which the groove extends is trapezoidal, and the longer lower base is formed closer to the shaft body 18 than the shorter upper base. In the cross section perpendicular to the direction in which the convex grooves extend, a lower base that is slightly smaller than the cross section of the concave grooves and longer than the upper base is formed at the other end in the thickness direction. The arm 13 holds the base plate 4 by fitting the convex groove of the base plate 4 and the concave groove of the holding portion 14 into each other. In the present embodiment, the transport means 5 is configured to include carbon.

アーム 13が下地板 4を保持した状態において、アーム 13が鉛直方向 Zに平行とな るときに、下地板 4の厚み方向の一表面部が融液 11に浸漬するように、アーム 13の 長さが設定される。またアーム 13が鉛直方向 Zに平行となるときに、下地板 4の厚み 方向の一表面 4aが融液 11の液面に対して平行となるように、アーム 13は、下地板 4 を保持する。  In a state where the arm 13 holds the base plate 4, the length of the arm 13 is adjusted so that one surface portion in the thickness direction of the base plate 4 is immersed in the melt 11 when the arm 13 is parallel to the vertical direction Z. Is set. Further, when the arm 13 is parallel to the vertical direction Z, the arm 13 holds the base plate 4 so that one surface 4a in the thickness direction of the base plate 4 is parallel to the liquid surface of the melt 11. .

基板製造装置 1は、収容空間 9に不活性ガスを供給するガス供給手段 15をさらに 備える。ガス供給手段 15が供給する不活性ガスは、たとえばアルゴンおよびヘリウム などの希ガスおよび窒素ガスなどから選択される。ガス供給手段 15は、チャンバ 3の 上方 Z1の上壁部に形成される 1または複数の不活性ガス流入孔 16に接続されるガ ス供給管を有する。ガス供給手段 15は、この不活性ガス流入孔 16から不活性ガスを チャンバ 3に供給する。本実施の形態では、 2つの不活性ガス流入孔 16がチャンバ 3 の上壁部に設けられ、この 2つの不活性ガス流入孔 16から不活性ガスが供給される 。本実施の形態では、ガス供給手段 15は、各不活性ガス流入孔 16からそれぞれ等 しい流量の不活性ガスを収容空間 9に供給する。ガス供給手段 15がチャンバ 3に不 活性ガスを供給することによって、収容空間 9に流入した酸素などのガスをチャンバ 3 から排気し、不活性ガスの雰囲気において基板 12を製造することができる。このよう に不活性ガスの雰囲気において基板 12を製造するので、融液 11が雰囲気中の酸 素などと反応して基板 12に不純物が混ざることを防ぐことができる。さらに運搬手段 5 および坩堝 2が酸化して消耗することを抑制することができる。図 1において、基板製 造装置 1における不活性ガスの流れを矢符 F1にて示す。 The substrate manufacturing apparatus 1 further includes gas supply means 15 that supplies an inert gas to the accommodation space 9. The inert gas supplied by the gas supply means 15 is selected from rare gases such as argon and helium and nitrogen gas, for example. The gas supply means 15 has a gas supply pipe connected to one or a plurality of inert gas inflow holes 16 formed in the upper wall portion of the upper Z1 of the chamber 3. The gas supply means 15 supplies the inert gas to the chamber 3 through the inert gas inflow hole 16. In the present embodiment, two inert gas inflow holes 16 are provided in the upper wall portion of the chamber 3, and the inert gas is supplied from the two inert gas inflow holes 16. In the present embodiment, the gas supply means 15 supplies an inert gas with an equal flow rate from the inert gas inflow holes 16 to the accommodation space 9. By supplying the inert gas to the chamber 3 by the gas supply means 15, the gas such as oxygen flowing into the accommodation space 9 can be exhausted from the chamber 3, and the substrate 12 can be manufactured in an inert gas atmosphere. like this In addition, since the substrate 12 is manufactured in an inert gas atmosphere, it is possible to prevent the melt 11 from reacting with oxygen in the atmosphere and mixing impurities into the substrate 12. Further, it is possible to suppress the transport means 5 and the crucible 2 from being oxidized and consumed. In FIG. 1, the flow of the inert gas in the substrate manufacturing apparatus 1 is indicated by an arrow F1.

本実施の形態では、チャンバ 3は、鉛直方向 Zに平行な予め定める第 2軸線 L2に 対して線対称に形成される。したがって、チャンバ 3に形成される 2つの不活性ガス流 入孔 16も予め定める第 2軸線 L2に対して線対称に形成される。前述したようにガス 供給手段 15は、各不活性ガス流入孔 16からそれぞれ等しい流量の不活性ガスを収 容空間 9に供給するので、収容空間 9を流れる不活性ガスも予め定める第 2軸線 L2 に対して線対称に流れる。  In the present embodiment, the chamber 3 is formed symmetrically with respect to a predetermined second axis L2 parallel to the vertical direction Z. Accordingly, the two inert gas inflow holes 16 formed in the chamber 3 are also formed symmetrically with respect to the predetermined second axis L2. As described above, the gas supply means 15 supplies the inert gas having the same flow rate from the inert gas inflow holes 16 to the storage space 9, so that the inert gas flowing through the storage space 9 is also determined in advance by the second axis L2 Flows symmetrically with respect to.

運搬手段 5は、軸体 18を第 1軸線 L1まわりの一方 F2に角変位しながら回転駆動す る駆動手段をさらに備える。各アーム 13は、搬送手段 7によって搬送される下地板 4 を保持しながら、駆動手段によって回転駆動される軸体 18とともに回転する。図 1で は、各アーム 13は、第 1軸線 L1まわりに反時計回りに回転する。アーム 13が第 1軸 線 L1まわりに回転することによって、アーム 13に保持された下地板 4が融液 11に浸 漬している間に、下地板 4の厚み方向の一表面 4aから融液 11が凝固成長することに よって基板 12が形成される。下地板 4が融液 11から離間すると、下地板 4は搬送手 段 7によって収容空間 9外に搬送される。  The transport means 5 further includes drive means for rotationally driving the shaft body 18 while angularly displacing the shaft body 18 to one F2 around the first axis L1. Each arm 13 rotates together with the shaft 18 that is driven to rotate by the driving means while holding the base plate 4 that is conveyed by the conveying means 7. In FIG. 1, each arm 13 rotates counterclockwise around the first axis L1. By rotating the arm 13 around the first axis L1, the base plate 4 held by the arm 13 is immersed in the melt 11 while the base plate 4 is immersed in the melt from one surface 4a in the thickness direction. Substrate 12 is formed by solidification growth of 11. When the base plate 4 is separated from the melt 11, the base plate 4 is transported out of the accommodation space 9 by the transport means 7.

下地板 4に形成される基板 12の厚みは、融液 11の温度および軸体 18の回転速度 などに依存する。この融液 11の温度および軸体 18の回転速度などは、中央処理装 置(Central Processing Unit:略称 CPU)などを含んで実現される制御手段によって 制御される。  The thickness of the substrate 12 formed on the base plate 4 depends on the temperature of the melt 11 and the rotational speed of the shaft 18. The temperature of the melt 11 and the rotational speed of the shaft 18 are controlled by control means realized including a central processing unit (abbreviated as CPU).

チャンバ 3には、バッファ室 6と連通する開口が形成される。下地板 4は、この開口を 通って収容空間 9に搬入される、または収容空間 9外に搬出される。また収容空間 9 のガスは、この開口を通って収容空間 9外に排気される。  An opening communicating with the buffer chamber 6 is formed in the chamber 3. The base plate 4 is carried into the accommodation space 9 through this opening or carried out of the accommodation space 9. The gas in the storage space 9 is exhausted out of the storage space 9 through this opening.

図 2は、図 1におけるセクション IIの拡大断面図である。バッファ室 6は、下地板 4を 収容空間 9に搬入するときに下地板 4が通過する第 1バッファ室(図 1において左側 に位置する)と、収容空間 9から下地板 4を搬出するときに通過する第 2バッファ室(図 1において右側に位置する)とを含んで構成される。第 1および第 2バッファ室 6は、同 じ構造を有し、前述した予め定める第 2軸線 L2に対して線対称に配置されるので、 第 1および第 2バッファ室 6をまとめて説明する。 FIG. 2 is an enlarged cross-sectional view of section II in FIG. The buffer chamber 6 includes a first buffer chamber (located on the left side in FIG. 1) through which the base plate 4 passes when the base plate 4 is carried into the storage space 9, and a base plate 4 when the base plate 4 is carried out of the storage space 9. Second buffer chamber (Figure) 1 on the right side). Since the first and second buffer chambers 6 have the same structure and are arranged symmetrically with respect to the above-described predetermined second axis L2, the first and second buffer chambers 6 will be described together.

バッファ室 6は、バッファ空間 25を形成するバッファ室本体 19と、バッファ室本体 19 のチャンバ 3に対向する一側壁 29からチャンバ 3に延びる連通管 20と、バッファ室本 体 19の連通管 20が設けられる一側壁 29に対向する他側壁 30からチャンバ 3とは反 対側に延びる搬送管 21と、バッファ室本体 19の上方 Z1の上壁 31から上方 Z1に延 びて排気管 8に接続される接続管 22とを含んで構成される。  The buffer chamber 6 includes a buffer chamber main body 19 that forms a buffer space 25, a communication pipe 20 that extends from the one side wall 29 facing the chamber 3 of the buffer chamber main body 19 to the chamber 3, and a communication pipe 20 of the buffer chamber main body 19. A transfer pipe 21 extending from the other side wall 30 facing the provided side wall 29 to the opposite side of the chamber 3, and an upper wall 31 of the upper Z1 of the buffer chamber body 19 extending from the upper wall 31 to the upper Z1 and connected to the exhaust pipe 8. Connecting pipe 22.

連通管 20によって形成される管路(以下、連通孔という) 17は、チャンバ 3に形成さ れる開口を通じて収容空間 9に連通し、バッファ空間 25は、この連通孔 17を通じて 収容空間 9に連通する。前述したように、ガス供給手段 15から供給される不活性ガス は、予め定める第 2軸線 L2に対して線対称に流れるので、各連通孔 17を通って各 バッファ空間 25にそれぞれ流入する不活性ガスの流量は等しくなる。複数の連通孔 17のうちの 1または複数の特定の連通孔 17を流れる不活性ガスの流量が少ない場 合、流量の少ない連通孔 17から外気が収容空間 9に流入し易くなる力 S、各連通孔 17 を流れる不活性ガスの流量がそれぞれ等しいので、収容空間 9にバッファ空間 25か ら外気が流入することを防ぐことができる。これによつて収容空間 9の酸素濃度を低減 すること力 Sでさる。  A pipe line (hereinafter referred to as a communication hole) 17 formed by the communication pipe 20 communicates with the accommodation space 9 through an opening formed in the chamber 3, and the buffer space 25 communicates with the accommodation space 9 through the communication hole 17. . As described above, since the inert gas supplied from the gas supply means 15 flows symmetrically with respect to the predetermined second axis L2, the inert gas flowing into the buffer spaces 25 through the communication holes 17 respectively. The gas flow is equal. When the flow rate of the inert gas flowing through one or more specific communication holes 17 out of the plurality of communication holes 17 is small, the force S that makes it easy for outside air to flow into the accommodation space 9 from the communication holes 17 with a low flow rate. Since the flow rates of the inert gas flowing through the communication hole 17 are the same, it is possible to prevent outside air from flowing into the accommodation space 9 from the buffer space 25. This reduces the oxygen concentration in the accommodation space 9 by the force S.

下地板 4は、搬送管 21によって形成される管路(以下、搬送孔という) 23を通って 基板製造装置 1外からバッファ空間 25に搬入される、または搬送孔 23を通ってバッ ファ空間 25から基板製造装置 1外に搬出される。  The base plate 4 is carried into the buffer space 25 from the outside of the substrate manufacturing apparatus 1 through the pipe line (hereinafter referred to as “transport hole”) 23 formed by the transport pipe 21, or the buffer space 25 through the transport hole 23. From outside the board manufacturing apparatus 1.

基板製造装置 1は、搬送孔 23を開閉可能な開閉手段 24をさらに備える。開閉手段 24は、バッファ室 6のチャンバ 3側とは反対側の端部、すなわち搬送管 21のバッファ 室本体 19側とは反対側の端部に近接して設けられる。開閉手段 24は、搬送孔 23を 開閉可能な薄い直方体つまり板状のシャツタ 33と、シャツタ 33の上方 Z1に設けられ るエアシリンダと、シャツタ 33とエアシリンダとを接続するロッドと、シャツタ 33の移動を 規制するリニアガイドとを含んで構成される。シャツタ 33は、金属材料および樹脂材 料などによって形成される。シャツタ 33は、リニアガイドによって鉛直方向 Zを除く方 向への動きが規制され、鉛直方向 Zにのみ移動可能に設けられる。エアシリンダが口 ッドを介してシャツタ 33を鉛直方向 Zに押圧または引張ることによって、シャツタ 33は 鉛直方向 Zに移動する。このようにシャツタ 33を鉛直方向 Zに移動することによって搬 送孔 23の開閉動作を行う。シャツタ 33は、厚み方向に垂直な断面が、少なくとも搬送 管 21の延びる方向に垂直な搬送孔 23の断面よりも大きく形成され、下方 Z2に移動 したときにシャツタ 33の厚み方向の一方から見て搬送孔 23を覆う形状に形成される。 このシャツタ 33は、下地板 4が搬送孔 23を通過するときには、上方 Z1に移動して搬 送孔 23を開状態にし、それ以外のときには下方 Z2に移動して搬送孔 23を閉状態に する。これによつて外気がバッファ空間 25に流入することを可及的に防いでいる。ま た開閉手段 24は、搬送管 21に近接して、すなわち搬送孔 23に近接して設けられる ので、開閉手段 24と搬送孔 23との隙間が狭くなる。したがつてこの隙間から空気など のガスが収容空間 9に流れ込むことを防ぐことができる。これによつて収容空間 9の酸 素濃度を低減することができ、基板 4に不純物が混入することを防ぐことができ、さら には基板製造装置 1の長寿命化を図ることができる。 The substrate manufacturing apparatus 1 further includes opening / closing means 24 that can open and close the transport hole 23. The opening / closing means 24 is provided close to the end of the buffer chamber 6 opposite to the chamber 3 side, that is, the end of the transfer tube 21 opposite to the buffer chamber body 19 side. The opening / closing means 24 includes a thin rectangular parallelepiped or plate-shaped shirt 33 capable of opening and closing the transport hole 23, an air cylinder provided above Z1 of the shirt 33, a rod connecting the shirt 33 and the air cylinder, and the shirt 33 And a linear guide that regulates movement. The shirt 33 is formed of a metal material and a resin material. The shirtta 33 is the one that removes the vertical direction Z by the linear guide. Movement in the direction is restricted, and it can be moved only in the vertical direction Z. When the air cylinder presses or pulls the shirt 33 in the vertical direction Z through the mouth, the shirt 33 moves in the vertical direction Z. In this way, the transport hole 23 is opened and closed by moving the shirt 33 in the vertical direction Z. The shirter 33 is formed so that a cross section perpendicular to the thickness direction is at least larger than a cross section of the transport hole 23 perpendicular to the direction in which the transport pipe 21 extends, and when viewed in one of the thickness directions of the shirter 33 when moved downward Z2. It is formed in a shape that covers the transport hole 23. When the base plate 4 passes through the transport hole 23, the shirt 33 moves to the upper Z1 to open the transport hole 23, and otherwise moves to the lower Z2 to close the transport hole 23. . This prevents outside air from flowing into the buffer space 25 as much as possible. Further, since the opening / closing means 24 is provided close to the transport pipe 21, that is, close to the transport hole 23, the gap between the open / close means 24 and the transport hole 23 is narrowed. Therefore, gas such as air can be prevented from flowing into the accommodation space 9 from this gap. As a result, the oxygen concentration in the accommodation space 9 can be reduced, impurities can be prevented from being mixed into the substrate 4, and the life of the substrate manufacturing apparatus 1 can be extended.

接続管 22は、バッファ室本体 19の上壁 31のチャンバ 3側とは反対側の端部から上 方 Z1に延びる。排気管 8は、各バッファ室 6にそれぞれ形成される接続管 22からそ れぞれ上方 Z1に延び、上方 Z1の端部からそれぞれチャンバ 3の上方 Z1にお!/、て連 結するように水平に延びて形成される。排気管 8の連結部 26の上方 Z1の上壁には、 開孔 27が形成される。ガス供給手段 15からチャンバ 3に供給される不活性ガスは、 チャンバ 3、連通孔 17、バッファ空間 25、接続管 22によって形成される管路 (以下、 排気孔という) 34、排気管 8によって形成される管路、および排気管 8の連結部 26に 形成される開孔 27をこの順に通って基板製造装置 1外に排気される。  The connection pipe 22 extends upward Z1 from the end of the upper wall 31 of the buffer chamber body 19 opposite to the chamber 3 side. The exhaust pipe 8 extends from the connecting pipe 22 formed in each buffer chamber 6 to the upper Z1, and is connected to the upper Z1 of the chamber 3 from the end of the upper Z1. It is formed extending horizontally. An opening 27 is formed in the upper wall of Z1 above the connecting portion 26 of the exhaust pipe 8. The inert gas supplied from the gas supply means 15 to the chamber 3 is formed by the chamber 3, the communication hole 17, the buffer space 25, a pipe line (hereinafter referred to as an exhaust hole) 34 formed by the connection pipe 22, and the exhaust pipe 8. Then, the air is exhausted out of the substrate manufacturing apparatus 1 through the pipe line and the opening 27 formed in the connecting portion 26 of the exhaust pipe 8 in this order.

本実施の形態では、バッファ室 6の容積、すなわちバッファ空間 25の容積と、連通 孔 17の容積と、搬送孔 23の容積と、排気孔 34の容積とを加算した容積は、チャンバ 3の容積、すなわち収容空間 9の容積の 0%を超えてかつ 10%以下に選ばれる。 , ッファ空間 25には、ガス供給手段 15から供給される不活性ガスが収容空間 9から流 入するので、バッファ空間 25の圧力は、少なくとも大気圧よりも高くなる。バッファ空 間 25の圧力が大気圧より高ければ、搬送孔 23が開のときに外気がバッファ空間 25 に流入することを防ぐことができる。バッファ室 6の容積がチャンバ 3の容積の 10%を 超えて大きい場合には、バッファ空間 25の圧力が高くなる作用が低下するので、大 気圧とバッファ空間 25の圧力との差が小さくなり、外気がバッファ空間 25に流入する ことを防ぐ効果が小さくなる。本実施の形態のようにバッファ室 6の容積がチャンバ 3 の容積に比べて十分に小さければ、バッファ室 6の容積が大きい場合に比べて、バッ ファ空間 25の圧力と大気圧との差が大きくなり、外気がバッファ室 6に流入することを 効率的に防ぐことができる。これによつてバッファ空間 25の酸素濃度を低減すること ができ、これにともなって収容空間 9の酸素濃度を低減することができる。 In the present embodiment, the volume of the buffer chamber 6, that is, the volume of the buffer space 25, the volume of the communication hole 17, the volume of the transfer hole 23, and the volume of the exhaust hole 34 is the volume of the chamber 3. That is, it is selected to exceed 0% and not more than 10% of the volume of the accommodating space 9. Since the inert gas supplied from the gas supply means 15 flows into the buffer space 25 from the storage space 9, the pressure in the buffer space 25 is at least higher than the atmospheric pressure. If the pressure in the buffer space 25 is higher than atmospheric pressure, the outside air will be in the buffer space 25 when the transfer hole 23 is open. Can be prevented. When the volume of the buffer chamber 6 is larger than 10% of the volume of the chamber 3, the effect of increasing the pressure in the buffer space 25 is reduced, so the difference between the atmospheric pressure and the pressure in the buffer space 25 is reduced. The effect of preventing outside air from flowing into the buffer space 25 is reduced. If the volume of the buffer chamber 6 is sufficiently smaller than the volume of the chamber 3 as in the present embodiment, the difference between the pressure in the buffer space 25 and the atmospheric pressure is larger than when the volume of the buffer chamber 6 is large. It becomes large and can effectively prevent outside air from flowing into the buffer chamber 6. As a result, the oxygen concentration in the buffer space 25 can be reduced, and accordingly, the oxygen concentration in the accommodation space 9 can be reduced.

搬送手段 7は、バッファ室 6に搬入される下地板 4を収容空間 9に設けられる運搬手 段 5に搬送する、または運搬手段 5によって運搬された下地板 4をバッファ室 6に搬送 する。搬送手段 7は、たとえば平行に延びる 2本のレールと、 2本のレールの延びる方 向に垂直な方向に延び、両端部が各レールに軸支される複数のシャフトと、各シャフ トに軸支され、シャフトの軸線方向に等間隔をあけて配置される複数の搬送ローラと、 各シャフトを軸線まわりに回転駆動する駆動体とを含んで構成される。各シャフトは、 2本のレールの延びる方向に等間隔をあけて配置される。各シャフトには、 3個以上 の円盤状の搬送ローラが設けられ、各搬送ローラは、シャフトとともに回転する。後述 するように搬送手段 7には、下方 Z2から上方 Z1に向けてガス噴出手段 35から不活 性ガスが噴出される。搬送ローラおよびシャフトは、それぞれガス噴出手段 35からの 不活性ガスの流れを乱さない程度に十分な間隔をあけて配置される。このように搬送 手段 7は、各シャフトが回転することによって、搬送手段 7の上方 Z1から搬送ローラに 載置される下地板 4を 2本のレールが延びる方向に搬送する。下地板 4の搬送方向 は、シャフトの回転方向によって切換わる。搬送手段 7によって運搬手段 5に搬送さ れる下地板 4は、前述したように運搬手段 5の保持部 14に嵌合して保持され、運搬手 段 5によって融液 11に浸漬されて搬送手段 7に運搬され、さらに搬送手段 7によって バッファ室 6に搬送される。  The transport means 7 transports the base plate 4 carried into the buffer chamber 6 to the transport means 5 provided in the accommodation space 9, or transports the base plate 4 transported by the transport means 5 to the buffer chamber 6. The conveying means 7 includes, for example, two rails extending in parallel, a plurality of shafts extending in a direction perpendicular to the extending direction of the two rails and having both ends pivotally supported by the rails, and shafts on the shafts. A plurality of transport rollers that are supported and are arranged at equal intervals in the axial direction of the shaft, and a drive body that rotationally drives each shaft around the axis. Each shaft is arranged at equal intervals in the extending direction of the two rails. Each shaft is provided with three or more disk-shaped transport rollers, and each transport roller rotates together with the shaft. As will be described later, an inert gas is ejected from the gas ejection means 35 to the transport means 7 from the lower Z2 toward the upper Z1. The conveying roller and the shaft are arranged at a sufficient interval so as not to disturb the flow of the inert gas from the gas ejection means 35. In this way, the conveying means 7 conveys the base plate 4 placed on the conveying roller from the upper Z1 of the conveying means 7 in the direction in which the two rails extend as each shaft rotates. The conveying direction of the base plate 4 is switched depending on the rotation direction of the shaft. The base plate 4 transported to the transport means 5 by the transport means 7 is fitted and held in the holding portion 14 of the transport means 5 as described above, and is immersed in the melt 11 by the transport means 5 and transported by the transport means 7. And is further transported to the buffer chamber 6 by the transport means 7.

図 3は、図 2の切断面線 III IIIから見たバッファ室 6の断面図である。基板製造装 置 1は、バッファ空間 25にガス噴出手段 35をさらに備える。ガス噴出手段 35は、バッ ファ空間 25で搬送孔 23寄りに近接して設けられる。具体的には、本実施の形態では ガス噴出手段 35は、バッファ室本体 19の下方 Z2の下壁 36上の搬送管 21寄りの端 部に設けられる。ガス噴出手段 35は、他側壁 30に沿って、他側壁 30の上下方向 Z に垂直な第 1方向 Xの両端部間にわたって延びる。ガス噴出手段 35の上方 Z1の端 部には、第 1方向 Xの両端部間にわたって延びる噴出孔が形成される。ガス噴出手 段 35は、噴出孔に不活性ガスを供給する不活性ガス供給源を備え、噴出孔から上 方 Z1に向けて不活性ガスを噴出する。本実施の形態では、ガス噴出手段 35の噴出 孔は、ガス噴出手段 35の延びる方向(第 1方向 X)に長手状の長孔であって、この噴 出孔に臨む内周面は、四角筒形状を有する。図 3では、ガス噴出孔から噴出する不 活性ガスの流れを矢符 38にて示す。前述したように接続管 22は、バッファ室本体 19 の上壁 31の搬送管 21寄りの端部に設けられるので、ガス噴出手段 35は、排気孔 34 の下方 Z2に位置し、排気孔 34に向けて不活性ガスを噴出する。 FIG. 3 is a cross-sectional view of the buffer chamber 6 as seen from the section line III III in FIG. The substrate manufacturing apparatus 1 further includes gas ejection means 35 in the buffer space 25. The gas ejection means 35 is provided in the buffer space 25 close to the transport hole 23. Specifically, in this embodiment, The gas jetting means 35 is provided at the end near the transfer pipe 21 on the lower wall 36 of the lower Z2 of the buffer chamber body 19. The gas ejection means 35 extends along the other side wall 30 between both ends of the first direction X perpendicular to the up-down direction Z of the other side wall 30. An ejection hole extending between both end portions in the first direction X is formed at the end portion of the upper Z1 of the gas ejection means 35. The gas ejection means 35 includes an inert gas supply source that supplies an inert gas to the ejection hole, and ejects the inert gas from the ejection hole toward the upper Z1. In the present embodiment, the ejection hole of the gas ejection means 35 is a long hole that is long in the extending direction of the gas ejection means 35 (first direction X), and the inner peripheral surface facing this ejection hole is a square. It has a cylindrical shape. In FIG. 3, the flow of the inert gas ejected from the gas ejection hole is indicated by an arrow 38. As described above, since the connection pipe 22 is provided at the end of the upper wall 31 of the buffer chamber body 19 near the transport pipe 21, the gas ejection means 35 is located below the exhaust hole 34 at Z2 and is connected to the exhaust hole 34. Inert gas is spouted out.

前述した搬送管 21は、四角筒状の形状を有し、バッファ室本体 19の他側壁 30に は搬送孔 23が連通する開口 37が形成される。この開口 37は、ガス噴出手段 35の延 びる方向と同様に第 1方向 Xに延び、上下方向 Zおよび第 1方向 Xに垂直な第 2方向 Yの一方から見て、ガス噴出手段 35の上方 Z1に形成される。またこの開口 37は、第 1方向 Xにおいて、ガス噴出孔の中央部に形成される。ガス噴出孔の延びる方向の 幅の寸法 W1 (以下、ガス噴出孔の長手方向の幅の寸法 W1という)は、他側壁 30に 形成される開口 37のガス噴出手段 35の延びる方向の幅の寸法 W2 (以下、開口 37 の長手方向の幅の寸法 W2という)よりも大きい値に選ばれ、好ましくは前記開口 37 の長手方向の幅の寸法 W2の 1. 5倍に選ばれる。すなわちガス噴出手段 35は、搬 送孔 23を規定する面つまり搬送孔 23に臨む搬送管 21の内周面を延長した仮想平 面によって囲まれる領域(図 3では、開口 37内の領域)に、前記領域の外方にわたつ てガスを噴出する。ガス噴出孔から噴出される不活性ガスの流れは、ガス噴出孔の延 びる方向の端部において乱れが生じるので、仮に前記領域のみにガスを噴出すると 、不活性ガスの流れに乱れが生じる部分にお!/、て搬送孔 23から流入する外気を効 果的に排気孔 34に排気することができない。ガス噴出手段 35は、前記領域の外方 にわたつてガスを噴出するので、前記領域にお!/、て不活性ガスの流れに乱れが生じ ず、搬送孔 23から流入する外気をより効果的に排気孔 34に排気することができる。 これによつて連通孔 17を通って収容空間 9に外気が流入することを防いで収容空間 9の酸素濃度を低減することができる。 The transport pipe 21 described above has a rectangular cylindrical shape, and an opening 37 through which the transport hole 23 communicates is formed on the other side wall 30 of the buffer chamber body 19. This opening 37 extends in the first direction X in the same manner as the direction in which the gas ejection means 35 extends, and is located above the gas ejection means 35 when viewed from one of the vertical direction Z and the second direction Y perpendicular to the first direction X. Formed in Z1. The opening 37 is formed in the center of the gas ejection hole in the first direction X. The width dimension W1 in the extending direction of the gas ejection holes (hereinafter referred to as the dimension W1 in the longitudinal direction of the gas ejection holes) is the width dimension in the extending direction of the gas ejection means 35 of the opening 37 formed in the other side wall 30. It is selected to be larger than W2 (hereinafter referred to as the dimension W2 in the longitudinal direction of the opening 37), preferably 1.5 times the dimension W2 in the longitudinal direction of the opening 37. That is, the gas ejection means 35 is in a region (a region in the opening 37 in FIG. 3) surrounded by a virtual plane that is an extension of the inner peripheral surface of the transport pipe 21 that faces the transport hole 23, that is, the transport hole 23. The gas is ejected to the outside of the region. Since the flow of the inert gas ejected from the gas ejection hole is disturbed at the end in the extending direction of the gas ejection hole, if the gas is ejected only to the region, the part of the inert gas flow is disturbed. However, the outside air flowing from the transfer hole 23 cannot be effectively exhausted to the exhaust hole 34. Since the gas jetting means 35 jets the gas to the outside of the area, there is no turbulence in the flow of inert gas in the area, and the outside air flowing in from the transfer hole 23 is more effective. The exhaust hole 34 can be exhausted. As a result, the outside air can be prevented from flowing into the accommodation space 9 through the communication hole 17 and the oxygen concentration in the accommodation space 9 can be reduced.

下地板 4は、搬送手段 7によって搬送孔 23を通ってバッファ空間 25に搬入されると きにガス噴出手段 35の上方 Z1を通過する。このときガス噴出手段 35は上方 Z1を通 過する下地板 4に向けて不活性ガスを噴出するので、下地板 4を覆って搬送される外 気を下地板 4から離間させる。図 2において酸素ガス 28を模式的に記号「〇」で示す とともに、ガス噴出手段 35から噴出される不活性ガスによって酸素ガス 28が流れる向 きを矢符 32にて示す。特に、前述したようにガス噴出手段 35は、バッファ空間 25で 搬送孔 23寄りに近接して設けられる。すなわちガス噴出手段 35は、バッファ空間 25 で連通孔 17寄りでなぐ搬送孔 23寄りにおいて下地板 4に不活性ガスを噴出する。 このように連通孔 17から離れた位置において下地板 4を覆う酸素などのガスを離間さ せるので、離間したガスが連通孔 17を通ることを極力防ぐことができ、外気が収容空 間 9に流れ込むことを防ぐことができる。これによつて収容空間 9の酸素濃度を低減す ること力 Sでさる。  The base plate 4 passes through the upper Z1 of the gas ejection means 35 when it is carried into the buffer space 25 through the conveyance hole 23 by the conveyance means 7. At this time, since the gas ejection means 35 ejects the inert gas toward the base plate 4 passing through the upper Z1, the outside air that covers and covers the base plate 4 is separated from the base plate 4. In FIG. 2, the oxygen gas 28 is schematically indicated by the symbol “◯”, and the direction in which the oxygen gas 28 flows by the inert gas ejected from the gas ejection means 35 is indicated by an arrow 32. In particular, as described above, the gas ejection means 35 is provided in the buffer space 25 close to the transport hole 23. That is, the gas jetting means 35 jets an inert gas to the base plate 4 in the buffer space 25 and in the vicinity of the transport hole 23 that is close to the communication hole 17. In this way, oxygen and other gases covering the base plate 4 are separated from each other at a position away from the communication hole 17, so that it is possible to prevent the separated gas from passing through the communication hole 17 as much as possible, and the outside air enters the accommodation space 9. It can be prevented from flowing. This reduces the oxygen concentration in the accommodation space 9 by the force S.

さらに、前述したようにガス噴出手段 35は、排気孔 34の下方 Z2に位置し、排気孔 3 4に向けて不活性ガスを噴出するので、バッファ空間 25において不活性ガスが渦を 巻いたり、滞留したりせずにガス噴出手段 35から排気孔 34に向力、う不活性ガスの流 れが生じる。この不活性ガスの流れに沿って、不活性ガスを噴出することによって下 地板 4から離間した酸素などのガスをスムーズに排気孔 34に運ぶことができる。これ によって下地板 4から離間した酸素などのガスが連通孔 17を通って収容空間 9に流 入することを防ぐこと力 Sできる。  Further, as described above, the gas ejection means 35 is located in the lower Z2 of the exhaust hole 34 and ejects the inert gas toward the exhaust hole 34, so that the inert gas swirls in the buffer space 25, The gas flows from the gas jetting means 35 to the exhaust hole 34 without stagnation, and a flow of inert gas is generated. By blowing out the inert gas along the flow of the inert gas, a gas such as oxygen separated from the base plate 4 can be smoothly conveyed to the exhaust hole 34. As a result, it is possible to prevent the gas such as oxygen separated from the base plate 4 from flowing into the accommodation space 9 through the communication hole 17.

さらに、シャツタ 33が開状態のときに搬送孔 23からバッファ空間 25に流入する外気 を、ガス噴出手段 35からのガスの流れに沿って排気孔 34に運ぶことができるので、 外気が連通孔 17を通って収容空間 9に流れ込むことを防ぐことができる。すなわちガ ス噴出手段 35から噴出される不活性ガスによって、外気が搬送孔 23からバッファ空 間 25および連通孔 17を通って収容空間 9に流入することを遮断する障壁(以下、不 活性ガス'カーテンという)が形成される。この不活性ガス 'カーテンは、 自身を通過す るガスを連通孔 17に運ぶ機能を有する。 ガス噴出手段 35のガス噴出孔の第 2方向 Yにおける寸法は、 0. 05mm以上かつ 0 . 2mm未満とするのが好ましい。ガス噴出孔の第 2方向 Yの寸法が 0. 05mm未満で あれば、流量が一定の場合に流速が高くなるので、少な!/、不活性ガスで効率的にガ スを冷却体に吹きつけることができる力 圧力損失が大きくなつて不活性ガスが流れ 難くなり、噴出孔の延びる方向における不活性ガスの流速が不均一になってしまうと いう問題がある。また、ガス噴出孔の第 2方向 Yの寸法が 0. 2mm以上であれば、流 量が一定の場合に流速が低くなるので、流速を高くする場合には不活性ガスの流量 が多くなり、不活性ガスの使用量が多くなつて基板の生産コストが高くなるという問題 がある。これらに加えて噴出孔を製造するときの公差を考慮すると、噴出孔の前記幅 の寸法が、 0. 05mm以上かつ 0. 2mm未満に設定することによって、不活性ガスの 流量を抑制するとともに、噴出孔の延びる方向における不活性ガスの流速を均一に すること力 Sでさる。 Furthermore, since the outside air flowing into the buffer space 25 from the transfer hole 23 when the shirt 33 is in the open state can be conveyed to the exhaust hole 34 along the gas flow from the gas ejection means 35, the outside air is communicated with the communication hole 17 It is possible to prevent the air from flowing into the accommodation space 9 through. That is, a barrier that blocks the outside air from flowing from the transfer hole 23 through the buffer space 25 and the communication hole 17 into the accommodating space 9 by the inert gas ejected from the gas ejection means 35 (hereinafter referred to as inert gas' A curtain) is formed. This inert gas curtain has a function of transporting gas passing through itself to the communication hole 17. The dimension in the second direction Y of the gas ejection hole of the gas ejection means 35 is preferably 0.05 mm or more and less than 0.2 mm. If the dimension of the gas injection hole in the second direction Y is less than 0.05 mm, the flow rate will be high when the flow rate is constant, so there will be little! /, And the inert gas will be used to efficiently blow the gas to the cooling body. Force that can be generated The pressure loss becomes large, and it becomes difficult for the inert gas to flow, and the flow rate of the inert gas in the direction in which the ejection holes extend becomes uneven. Also, if the dimension of the gas injection hole in the second direction Y is 0.2 mm or more, the flow rate is low when the flow rate is constant, so the flow rate of the inert gas increases when the flow rate is high. There is a problem that the production cost of the substrate becomes high due to the large amount of inert gas used. In addition to these, considering the tolerances when manufacturing the ejection holes, the flow size of the ejection holes is controlled by setting the width dimension of the ejection holes to 0.05 mm or more and less than 0.2 mm, The force S is used to make the flow rate of the inert gas uniform in the direction in which the jet hole extends.

不活性ガス 'カーテンの効果について実験結果に基づいて説明する。図 4は、ガス 噴出手段 35から噴出される不活性ガスの流量と、収容空間 9の酸素濃度との関係を 示す図である。図 4において、横軸はガス噴出手段 35から噴出される不活性ガスの 流量 (以下、カーテン流量という)を示し、縦軸は収容空間 9の酸素濃度を示す。図 4 に示す酸素濃度の測定結果は、ガス供給手段 15から収容空間 9に供給される不活 性ガスの流量(以下、チャンバ流量という)を 200L/minとしたときの測定値である。 図 4に示すように、カーテン流量が多くなる程、収容空間 9の酸素濃度が低下するこ とから、不活性ガス 'カーテンが収容空間 9に流入する外気を遮断する障壁として機 能すること力 S示される。図 4においてカーテン流量が 20L/min未満になると、収容 空間 9の酸素濃度が急上昇し、不活性ガス 'カーテンの遮断効果が実用に適する程 度に有効に機能しないことが示される。カーテン流量が 20L/min以上になると、収 容空間 9の酸素濃度を 35ppm程度未満に保つことができるので、不活性ガス 'カー テンが収容空間 9に流入する外気を遮断する障壁として機能する効果が顕著に現れ ること力 S示される。特に、カーテン流量が 100L/min以上になると、収容空間 9の酸 素濃度を 5ppm以下に保つことができるので、不活性ガス 'カーテンが収容空間 9に 流入する外気を遮断する障壁として機能する効果が特に顕著に現れることが示され る。したがって、本実施の形態の基板製造装置 1では、カーテン流量は、 20L/min 以上に選ばれ、好ましくは、 100L/min以上に選ばれる。 The effect of the inert gas curtain will be explained based on experimental results. FIG. 4 is a diagram showing the relationship between the flow rate of the inert gas ejected from the gas ejection means 35 and the oxygen concentration in the accommodation space 9. In FIG. 4, the horizontal axis represents the flow rate of the inert gas ejected from the gas ejection means 35 (hereinafter referred to as curtain flow rate), and the vertical axis represents the oxygen concentration in the accommodation space 9. The measurement results of the oxygen concentration shown in FIG. 4 are measured values when the flow rate of the inert gas supplied from the gas supply means 15 to the accommodation space 9 (hereinafter referred to as the chamber flow rate) is 200 L / min. As shown in Fig. 4, as the curtain flow rate increases, the oxygen concentration in the containment space 9 decreases, so that the inert gas' curtain can function as a barrier to block outside air flowing into the containment space 9. S indicated. In Fig. 4, when the curtain flow rate is less than 20 L / min, the oxygen concentration in the containment space 9 rapidly increases, indicating that the inert gas' curtain blocking effect does not function as effectively as practical. When the curtain flow rate is 20 L / min or more, the oxygen concentration in the storage space 9 can be kept below about 35 ppm, so that the inert gas' curtain functions as a barrier that blocks outside air flowing into the storage space 9. The power S is shown to be noticeable. In particular, when the curtain flow rate is 100 L / min or more, the oxygen concentration in the containing space 9 can be kept at 5 ppm or less, so that the inert gas' curtain functions as a barrier that blocks outside air flowing into the containing space 9. Is shown to be particularly prominent The Therefore, in the substrate manufacturing apparatus 1 of the present embodiment, the curtain flow rate is selected to be 20 L / min or more, preferably 100 L / min or more.

一般にチャンバ 3、バッファ室 6および各孔などの基板製造装置 1の形状が異なると 、カーテン流量と収容空間 9の酸素濃度との相関は異なる力 S、流体力学の理論によ れば、次の式(1 )および式(2)でそれぞれ定義されるレイノルズ数 Reおよびシュミット 数 Scが等しければ、流速分布および濃度分布の相似則から、流れの速度分布およ び濃度分布がそれぞれ相似になる。したがって収容空間 9の酸素濃度は、基板製造 装置 1の形状に拘わらずに、レイカレズ数 Reおよびシュミット数 Scに依存するものと 推定される。  In general, if the shape of the substrate manufacturing apparatus 1 such as the chamber 3, the buffer chamber 6, and each hole is different, the correlation between the curtain flow rate and the oxygen concentration in the accommodating space 9 is different. If the Reynolds number Re and the Schmidt number Sc defined in Eq. (1) and Eq. (2) are equal, the flow velocity distribution and concentration distribution are similar from the flow velocity and concentration distribution similarity rules. Therefore, it is estimated that the oxygen concentration in the accommodation space 9 depends on the Reikarez number Re and the Schmitt number Sc regardless of the shape of the substrate manufacturing apparatus 1.

Re = UL/ r …ひ)  Re = UL / r… hi)

Sc = v /O · ' · (2)  Sc = v / O · '· (2)

レイノルズ数 Reおよびシュミット数 Scは、無次元数である。式(1 )において、 Uは、 代表流速(単位 m/s)を示し、 Lは、代表長さ { 4 X開口面積/開口部の周長(単位 m) }を示し、 Vは、不活性ガスの動粘性係数(単位 m2/s)を示す。また、式(2)にお いて、 Vは、不活性ガスの動粘性係数(単位 m2/s)を示し、 Dは、酸素の不活性ガス に対する拡散係数 (単位 m2/s)を示す。 The Reynolds number Re and the Schmidt number Sc are dimensionless numbers. In formula (1), U represents the representative flow velocity (unit m / s), L represents the representative length {4 X opening area / opening circumference (unit m)}, and V is inert. Indicates the kinematic viscosity coefficient (unit m 2 / s) of gas. In equation (2), V represents the kinematic viscosity coefficient (unit m 2 / s) of the inert gas, and D represents the diffusion coefficient (unit m 2 / s) of oxygen to the inert gas. .

基板製造装置 1の形状を変更したとしても、不活性ガスの種類を変更しない場合に は、不活性ガスと酸素との組合せは変わらないので、シュミット数 Scは常に変わらず に一定となる。したがってレイカレズ数 Reが同じであれば、収容空間 9の酸素濃度は 、基板製造装置 1の形状に拘わらずに等しくなると推定される。すなわち基板製造装 置 1の形状が異なっても、収容空間 9の酸素濃度とレイカレズ数 Reとの相関は同じで あると推定される。 目的とする収容空間 9の酸素濃度からレイカレズ数 Reが定められ 、基板製造装置 1の形状から代表長さ Lが求まるので、式(1 )から代表流速 Uを求め ること力 Sできる。代表流速 Uが求まると、ガス噴出手段 35から噴出すべきカーテン流 量を決定することができる。  Even if the shape of the substrate manufacturing apparatus 1 is changed, if the type of the inert gas is not changed, the combination of the inert gas and oxygen does not change, so the Schmitt number Sc is always unchanged and constant. Therefore, if the Reikarezu number Re is the same, the oxygen concentration in the accommodation space 9 is estimated to be equal regardless of the shape of the substrate manufacturing apparatus 1. That is, even if the shape of the substrate manufacturing apparatus 1 is different, it is estimated that the correlation between the oxygen concentration in the accommodation space 9 and the Reikarezu number Re is the same. Since the Reikarezu number Re is determined from the oxygen concentration of the target accommodating space 9 and the representative length L is obtained from the shape of the substrate manufacturing apparatus 1, the force S for obtaining the representative flow velocity U from the equation (1) can be obtained. When the representative flow velocity U is obtained, the curtain flow rate to be ejected from the gas ejection means 35 can be determined.

本実施の形態では、各バッファ室 6の連通孔 17は 1ケ所で、ガス噴出手段 35のガス 噴出孔のサイズは 500mm X O. 1mmなので、たとえばカーテン流量が l OOL/min のときのガス噴出手段 35のレイノルズ数 Re (以下、カーテン.レイノルズ数 Reという) は、 460となり、カーテン流量が 20L/minのときのカーテン ·レイノルズ数 Reは、 92 となる。上述した実験結果をカーテン 'レイカレズ数 Reを基準にして解析すると、カー テン.レイノルズ数 Reが 460以上の場合、不活性ガス.カーテンの遮断効果によって 収容空間 9の酸素濃度は 5ppm以下に保たれる。カーテン 'レイカレズ数 Reが 460未 満になると収容空間 9の酸素濃度が上昇を開始し、カーテン'レイカレズ数 Reが減少 するにしたがって収容空間 9の酸素濃度が上昇していき、最終的にカーテン 'レイノ ルズ数 Reが 92未満になると酸素濃度が急上昇し、不活性ガス 'カーテンの遮断効果 が実用に適する程度に有効に機能しなくなることが示される。したがって、基板製造 装置 1の形状に拘わらずに、カーテン 'レイカレズ数 Reは、 92以上に選ばれ、好まし くは、 460以上に選ばれる。 In this embodiment, there is one communication hole 17 in each buffer chamber 6, and the size of the gas ejection hole of the gas ejection means 35 is 500 mm X O. 1 mm. For example, the gas ejection when the curtain flow rate is l OOL / min. Reynolds number Re of means 35 (hereinafter referred to as curtain. Reynolds number Re) The curtain Reynolds number Re is 92 when the curtain flow rate is 20L / min. Analyzing the above experimental results based on the curtain 'Reikarez number Re, when the curtain Reynolds number Re is 460 or more, the oxygen concentration in the containment space 9 is kept below 5 ppm due to the shielding effect of the inert gas curtain. It is. Curtain 'When the Reikarez number Re is less than 460, the oxygen concentration in the containment space 9 starts to rise, and as the curtain' Reikarez number Re decreases, the oxygen concentration in the containment space 9 increases, and finally the curtain ' When the Reynolds number Re is less than 92, the oxygen concentration increases rapidly, indicating that the inert gas curtain blocking effect does not function as effectively as practical. Therefore, regardless of the shape of the substrate manufacturing apparatus 1, the curtain “Reikarezu number Re” is selected to be 92 or more, and preferably 460 or more.

同様にして、ガス供給手段 15によって収容空間 9に不活性ガスを供給することによ る効果について実験結果に基づいて説明する。図 5は、チャンバ流量と、収容空間 9 の酸素濃度との関係を示す図である。図 5において、横軸はチャンバ流量を示し、縦 軸は収容空間 9の酸素濃度を示す。図 5に示す酸素濃度の測定結果は、カーテン流 量を 100L/minとしたときの測定値である。  Similarly, the effect of supplying the inert gas to the accommodation space 9 by the gas supply means 15 will be described based on the experimental results. FIG. 5 is a diagram showing the relationship between the chamber flow rate and the oxygen concentration in the accommodation space 9. In FIG. 5, the horizontal axis indicates the chamber flow rate, and the vertical axis indicates the oxygen concentration in the accommodation space 9. The oxygen concentration measurement results shown in Fig. 5 are measured when the curtain flow rate is 100 L / min.

図 5に示すように、チャンバ流量が多くなる程、収容空間 9の酸素濃度が低下するこ とから、ガス供給手段 15によって収容空間 9に供給される不活性ガス力 S、収容空間 9 に外気が流入することを防ぐとともに、収容空間 9に流入した外気を収容空間 9外に 排気し、収容空間 9の酸素濃度を低下する排気効果を示すことが示される。図 5にお いてチャンバ流量が 100L/min未満になると、収容空間 9の酸素濃度が急上昇し、 ガス供給手段 15から供給される不活性ガスによる排気効果が実用に適する程度に 有効に機能しないことが示される。チャンバ流量が 100L/min以上になると、収容 空間 9の酸素濃度を 70ppm程度未満に保つことができるので、ガス供給手段 15から 供給される不活性ガスによる排気効果が顕著に現れることが示される。特に、チャン バ流量が 300L/min以上になると、収容空間 9の酸素濃度を約 lOppm以下に保つ ことができるので、ガス供給手段 15から供給される不活性ガスによる排気効果が特に 顕著に現れることが示される。したがって、本実施の形態の基板製造装置 1では、チ ヤンバ流量は、 100L/min以上に選ばれ、好ましくは、 300L/min以上に選ばれ 以上説明した実験結果を、不活性ガス 'カーテンの場合と同様に流速分布および 濃度分布の相似則にしたがって、レイカレズ数 Reを基準にして解析する。本実施の 形態では、各バッファ室 6の連通孔 17が 1ケ所で、そのサイズは 400mm X 100mm なので、たとえばチャンバ流量が 300L/minのときの連通孔 17のレイノルズ数 Re ( 以下、チャンノ 'レイノルズ数 Reという)は、 1100となり、チャンバ流量が 200L/min のときのチャンノ 'レイノルズ数 Reは、 734となり、チャンバ流量が 150L/minのとき のチャンノ 'レイノルズ数 Reは、 550となり、チャンバ流量が 100L/minのときのチヤ ンノ 'レイノルズ数 Reは、 367となる。チャンノ 'レイノルズ数 Reが 1100以上の場合、 排気効果によって酸素濃度は lOppm程度に保たれる。チャンバ 'レイカレズ数 Reが 1100未満になると酸素濃度が上昇を開始し、チャンバ 'レイカレズ数 Reが減少する にしたがって酸素濃度が上昇していき、最終的にチャンバ ·レイカレズ数 Reが 367未 満になると排気効果が実用に適する程度に有効に機能しなくなることが示される。し たがって、基板製造装置 1の形状に拘わらずに、チャンバ 'レイカレズ数 Reは、 367 以上に選ばれ、好ましくは、 1100以上に選ばれる。 As shown in FIG. 5, as the chamber flow rate increases, the oxygen concentration in the accommodation space 9 decreases, so that the inert gas force S supplied to the accommodation space 9 by the gas supply means 15 and the outside air in the accommodation space 9 It is shown that the outside air flowing into the storage space 9 is exhausted out of the storage space 9 and the oxygen concentration in the storage space 9 is reduced. In FIG. 5, when the chamber flow rate becomes less than 100 L / min, the oxygen concentration in the storage space 9 increases rapidly, and the exhaust effect of the inert gas supplied from the gas supply means 15 does not function effectively to a practical level. Is shown. When the chamber flow rate is 100 L / min or more, the oxygen concentration in the accommodation space 9 can be kept below about 70 ppm, which indicates that the exhaust effect by the inert gas supplied from the gas supply means 15 appears remarkably. In particular, when the chamber flow rate is 300 L / min or more, the oxygen concentration in the accommodation space 9 can be kept at about 10 ppm or less, and the exhaust effect by the inert gas supplied from the gas supply means 15 is particularly noticeable. Is shown. Therefore, in the substrate manufacturing apparatus 1 of the present embodiment, the chamber flow rate is selected to be 100 L / min or more, preferably 300 L / min or more. The experimental results described above are analyzed based on the Reikarezu number Re according to the similar law of flow velocity distribution and concentration distribution as in the case of the inert gas curtain. In this embodiment, each buffer chamber 6 has one communication hole 17 and the size thereof is 400 mm × 100 mm. For example, when the chamber flow rate is 300 L / min, the Reynolds number Re (hereinafter referred to as “Channo Reynolds”). The Reno's number Re is 734 when the chamber flow rate is 200 L / min, and the Channo Reynolds number Re is 550 when the chamber flow rate is 150 L / min. At the time of 100 L / min, the Cyanno Reynolds number Re is 367. When the Channo Reynolds number Re is 1100 or more, the oxygen concentration is kept at about lOppm by the exhaust effect. When the chamber 'Reikarezu number Re is less than 1100, the oxygen concentration starts to increase, and as the chamber' Reikarezu number Re decreases, the oxygen concentration increases. It is shown that the exhaust effect does not function as effectively as is practical. Therefore, regardless of the shape of the substrate manufacturing apparatus 1, the chamber “recalls number Re is selected to be 367 or more, and preferably 1100 or more.

以上説明したように、 目標とする収容空間 9の酸素濃度が決まれば、この酸素濃度 を達成するためのカーテン 'レイノルズ数 Reおよびチャンノ 'レイノルズ数 Reがそれ ぞれ図 4および図 5を基にして決定される。式(1)を用いると、カーテン 'レイカレズ数 Reおよびチャンバ ·レイカレズ数 Reから、新たに設計した基板製造装置 1に対してガ ス噴出孔から流れる不活性ガスの代表流速 Uおよび収容空間 9から連通孔 17を通る 不活性ガスの代表流速 Uを計算することができ、その流速に開口面積を乗算すること によって、カーテン流量およびチャンバ流量をそれぞれ見積もることが可能になる。こ のように設計時においてカーテン流量およびチャンバ流量を予め見積ることが可能と なり、不活性ガスの使用量と収容空間 9の酸素濃度とを考慮した設計が可能となる。 以上説明した本実施の形態の基板製造装置 1によれば、ガス供給手段 15によって 収容空間 9に供給された不活性ガスは、連通孔 17を通ってバッファ空間 25に流入し 、排気孔 34を通ってバッファ空間 25から排気される。したがって、収容空間 9に酸素 などのガスが流入したとしても、この不活性ガスの流れに沿って流入したガスを収容 空間 9およびバッファ空間 25から排気することができ、収容空間 9を不活性ガスによ つて満たすことができる。 As explained above, once the oxygen concentration in the target containment space 9 is determined, the curtains 'Reynolds number Re and Channo' Reynolds number Re to achieve this oxygen concentration are based on Figs. 4 and 5, respectively. Determined. Using equation (1), from the curtain 'Reikarezu number Re and chamber Reikarezu number Re, from the newly designed substrate manufacturing equipment 1 from the representative flow velocity U of the inert gas flowing from the gas ejection holes and from the accommodation space 9 The typical flow rate U of the inert gas passing through the communication hole 17 can be calculated, and the curtain flow rate and the chamber flow rate can be estimated by multiplying the flow rate by the opening area. In this way, the curtain flow rate and the chamber flow rate can be estimated in advance at the time of design, and the design can be made in consideration of the amount of inert gas used and the oxygen concentration of the storage space 9. According to the substrate manufacturing apparatus 1 of the present embodiment described above, the inert gas supplied to the accommodation space 9 by the gas supply means 15 flows into the buffer space 25 through the communication hole 17 and passes through the exhaust hole 34. It is exhausted from the buffer space 25 through. Therefore, even if a gas such as oxygen flows into the storage space 9, the gas flowing in along this inert gas flow is stored. The space 9 and the buffer space 25 can be evacuated, and the containing space 9 can be filled with an inert gas.

またシャツタ 33は、搬送孔 23を下地板 4が通過するときに搬送孔 23を開き、下地板 4が搬送孔 23を通過しないときには搬送孔 23を閉じる。これによつて下地板 4が搬送 孔 23を通過しないときに、バッファ空間 25に空気などの外気が流入することを防ぐこ と力 Sできる。また搬送孔 23が開いているときにバッファ空間 25に空気などの外気が流 入したとしても、流入したガスは、収容空間 9からバッファ空間 25を通って排気孔に 流れる不活性ガスの流れとともに排気孔 34から排気されるので、収容空間 9に外気 力流入することを防ぐこと力できる。  The shirt 33 opens the transport hole 23 when the base plate 4 passes through the transport hole 23, and closes the transport hole 23 when the base plate 4 does not pass through the transport hole 23. Accordingly, it is possible to prevent the outside air such as air from flowing into the buffer space 25 when the base plate 4 does not pass through the transport hole 23. Even if outside air such as air flows into the buffer space 25 when the transfer hole 23 is open, the inflowing gas flows along with the flow of inert gas flowing from the storage space 9 through the buffer space 25 to the exhaust hole. Since the air is exhausted from the exhaust hole 34, it is possible to prevent the outside air from flowing into the housing space 9.

またガス噴出手段 35は、バッファ空間 25において搬送される下地板 4に向けて不 活性ガスを噴出する。下地板 4に不活性ガスを噴出することによって、基板製造装置 1外からバッファ空間 25に搬入される下地板 4とともに移動し、下地板 4を覆う酸素な どのガスを下地板 4から離間させることができる。このようにして下地板 4から離れたガ スは、収容空間 9からバッファ空間 25を通って排気孔 34に流れる不活性ガスの流れ とともに排気孔 34から排気されるので、下地板 4を収容空間 9に搬送するときに外気 などが収容空間 9に流入することを防ぐことができる。このように真空環境用の装置を 備えることなぐ簡易な構成で収容空間 9に外気が流入することを防いで、収容空間 9を不活性ガスで満たすことができ、酸素濃度を低!/、値に抑えた不活性ガスの雰囲 気中において基板を製造することができる。これによつて融液 1 1が凝固成長するとき に基板 12に不純物が混入することを防ぐことができる。さらに収容空間 9に外気が流 入することを防!/、で収容空間 9の酸素濃度を低!/、値に抑えることができるので、高温 となる坩堝 2などの収容空間 9に設けられる装置およびチャンバが酸化して消耗する ことを防ぐことができ、基板製造装置 1の長寿命化を図ることができる。特に本実施の 形態では、坩堝 2および運搬手段 5は、カーボンを含んで形成されるので、収容空間 9の酸素濃度を低い値に抑えることによって、坩堝 2および運搬手段 5が酸化して消 耗することを防ぐことができる。従来の技術の基板製造装置 101のように真空環境用 の装置を備えることなぐ簡易な構成で収容空間 9の酸素濃度を低い値に抑えること ができるので、基板製造装置 1の小形化を実現して設置面積が小さくなり、低コストの 基板製造装置 1を実現することができる。 The gas ejection means 35 ejects an inert gas toward the base plate 4 conveyed in the buffer space 25. By injecting an inert gas onto the base plate 4, it moves with the base plate 4 carried into the buffer space 25 from the outside of the substrate manufacturing apparatus 1, and gas such as oxygen covering the base plate 4 is separated from the base plate 4. Can do. The gas thus separated from the base plate 4 is exhausted from the exhaust hole 34 together with the flow of the inert gas flowing from the storage space 9 through the buffer space 25 to the exhaust hole 34, so that the base plate 4 is stored in the storage space. It is possible to prevent outside air or the like from flowing into the accommodation space 9 when transported to the housing 9. In this way, it is possible to prevent outside air from flowing into the storage space 9 with a simple configuration without providing a device for a vacuum environment, so that the storage space 9 can be filled with an inert gas, and the oxygen concentration is reduced! The substrate can be manufactured in an inert gas atmosphere kept at a minimum. This prevents impurities from being mixed into the substrate 12 when the melt 11 is solidified and grown. Furthermore, since the oxygen concentration in the storage space 9 can be reduced to a low value by preventing the outside air from flowing into the storage space 9, a device provided in the storage space 9 such as the crucible 2 that is hot. In addition, the chamber can be prevented from being oxidized and consumed, and the life of the substrate manufacturing apparatus 1 can be extended. In particular, in the present embodiment, the crucible 2 and the transporting means 5 are formed to contain carbon, so that the crucible 2 and the transporting means 5 are oxidized and consumed by suppressing the oxygen concentration in the accommodation space 9 to a low value. Can be prevented. Since the oxygen concentration in the housing space 9 can be suppressed to a low value with a simple configuration that does not include an apparatus for a vacuum environment like the substrate manufacturing apparatus 101 of the prior art, the substrate manufacturing apparatus 1 can be downsized. The installation area is reduced and the cost is low. The board manufacturing apparatus 1 can be realized.

本実施の形態の基板製造装置 1では、ガス噴出手段 35は、バッファ室本体 19の下 方 Z2の下壁 36上に設けられて、上方 Z1に不活性ガスを噴出するとしたけれども、下 地板 4および排気孔 34に向けて不活性ガスを噴出するのであれば、どの位置に配 置されてもよい。  In the substrate manufacturing apparatus 1 of the present embodiment, the gas jetting means 35 is provided on the lower wall 36 of the lower Z2 of the buffer chamber body 19 and jets an inert gas to the upper Z1. As long as the inert gas is ejected toward the exhaust hole 34, it may be disposed at any position.

図 6は、ガス噴出手段 35をバッファ室本体 19の第 1方向 Xの一側壁 39に設けたと きのバッファ室 6の断面図である。ガス噴出手段 35をバッファ室本体 19の第 1方向 X の一側壁 39に設ける場合には、接続管 22は、バッファ室本体 19の第 1方向 Xの他 側壁 40から第 1方向 Xの他方に延びて形成される。ガス噴出手段 35は、排気管 8に 向けて第 1方向 Xの他方に不活性ガスを噴出する。ガス噴出手段 35は、バッファ室 本体 19の第 1方向 Xの一側壁 39の搬送管 21寄りの端部に設けられる。ガス噴出手 段 35は、一側壁 39に沿って、一側壁 39の上下方向 Zの両端部間にわたって延びる 。ガス噴出手段 35の第 1方向の他方の端部には、上下方向 Zの両端部間にわたって 延びる噴出孔が形成される。ガス噴出手段 35は、この噴出孔から第 1方向 Xの他方 に向けて不活性ガスを噴出する。ガス噴出手段 35の噴出孔は、ガス噴出手段 35の 延びる方向(上下方向 Z)に長手状の長孔であって、この噴出孔に臨む内周面は、四 角筒形状を有する。図 6では、ガス噴出孔から噴出する不活性ガスの流れを矢符 41 にて示す。  FIG. 6 is a cross-sectional view of the buffer chamber 6 when the gas ejection means 35 is provided on the one side wall 39 in the first direction X of the buffer chamber body 19. When the gas ejection means 35 is provided on one side wall 39 in the first direction X of the buffer chamber body 19, the connecting pipe 22 is connected from the other side wall 40 in the first direction X to the other side in the first direction X of the buffer chamber body 19. It is formed to extend. The gas ejection means 35 ejects an inert gas to the other side in the first direction X toward the exhaust pipe 8. The gas ejection means 35 is provided at the end of the one side wall 39 of the buffer chamber body 19 near the transfer pipe 21 in the first direction X. The gas ejection means 35 extends along the one side wall 39 between both end portions in the vertical direction Z of the one side wall 39. At the other end portion in the first direction of the gas ejection means 35, an ejection hole extending between both end portions in the vertical direction Z is formed. The gas ejection means 35 ejects an inert gas from the ejection hole toward the other side in the first direction X. The ejection hole of the gas ejection means 35 is a long hole that is long in the extending direction (vertical direction Z) of the gas ejection means 35, and the inner peripheral surface facing the ejection hole has a rectangular cylindrical shape. In FIG. 6, the flow of the inert gas ejected from the gas ejection holes is indicated by arrows 41.

前述したようにバッファ室本体 19の第 2方向 Yの他側壁 30には搬送孔 23による開 口 37力 S形成される。この開口 37は、第 1方向 Xに延び、第 2方向 Yの一方から見て、 ガス噴出手段 35の第 1方向 Xの他方に形成される。またこの開口 37は、上下方向 Z において、ガス噴出孔の中央部に形成される。ガス噴出孔の延びる方向の幅の寸法 W3 (以下、ガス噴出孔の長手方向の幅の寸法 W3という)は、他側壁 30に形成され る開口 37のガス噴出手段 35の延びる方向の幅の寸法 W4 (以下、開口 37の短手方 向の幅の寸法 W4という)よりも大きい値に選ばれ、好ましくは前記開口 37の短手方 向の幅の寸法 W4の 1. 5倍に選ばれる。このようにガス噴出孔の形状を設計すること によって、前述したように搬送孔 23を規定する面つまり搬送孔 23に臨む搬送管 21の 内周面を延長した仮想平面によって囲まれる領域(図 6では、開口 37内の領域)に おいて不活性ガスの流れに乱れが生じず、搬送孔 23から流入する外気を効果的に 排気孔 34に排気することができる。これによつて連通孔 17を通って収容空間 9に外 気が流入することを防いで収容空間 9の酸素濃度を低減することができる。 As described above, the opening 37 force S is formed on the other side wall 30 in the second direction Y of the buffer chamber body 19 by the transfer hole 23. The opening 37 extends in the first direction X, and is formed in the other of the gas ejection means 35 in the first direction X as viewed from one of the second directions Y. The opening 37 is formed at the center of the gas ejection hole in the vertical direction Z. The width dimension W3 in the extending direction of the gas ejection hole (hereinafter referred to as the dimension W3 in the longitudinal direction of the gas ejection hole) is the width dimension in the extending direction of the gas ejection means 35 of the opening 37 formed in the other side wall 30. It is selected to be larger than W4 (hereinafter referred to as the width dimension W4 of the opening 37), preferably 1.5 times the width W4 of the opening 37 in the width direction. By designing the shape of the gas ejection hole in this way, as described above, the area surrounded by the virtual plane extending the surface defining the transport hole 23, that is, the inner peripheral surface of the transport pipe 21 facing the transport hole 23 (FIG. 6). In the area in the opening 37) In this case, the flow of the inert gas is not disturbed, and the outside air flowing from the transfer hole 23 can be effectively exhausted to the exhaust hole 34. As a result, the outside air can be prevented from flowing into the accommodation space 9 through the communication hole 17 and the oxygen concentration in the accommodation space 9 can be reduced.

本実施の形態では、下地板 4の基板 12が形成される表面 4aに対して平行な方向 から、すなわち板状の下地板 4の面積が小さい面に対して垂直な方向から、不活性 ガスが噴射されることになる。このため、下地板 4の基板 12が形成される表面 4aと、こ の表面 4aに対向する表面とに均等に不活性ガスが噴射されて、表面 4aに対向する 表面を覆って搬送される外気も、速やかにかつ確実に排除することができる。さらに、 不活性ガスの流れの下地板 4による乱れも生じ難い。  In the present embodiment, the inert gas is generated from the direction parallel to the surface 4a of the base plate 4 on which the substrate 12 is formed, that is, from the direction perpendicular to the surface of the plate-like base plate 4 having a small area. Will be injected. For this reason, the inert gas is sprayed evenly on the surface 4a of the base plate 4 on which the substrate 12 is formed and the surface facing the surface 4a, and the outside air conveyed over the surface facing the surface 4a. Can be quickly and reliably eliminated. Furthermore, disturbance of the inert gas flow by the base plate 4 is unlikely to occur.

また本実施の形態の基板製造装置 1では、チャンバ 3およびバッファ室 6が第 2軸 線 L2に対して線対称に形成されるとしたけれども、線対称でなくてもよい。この場合 には、ガス供給手段 15は、各不活性ガス流入孔 16から流れる不活性ガスの流量を 調整することによって、各バッファ室 6の連通孔 17を通って各バッファ空間 25にそれ ぞれ流入する不活性ガスの流量が等しくなるように収容空間 9に不活性ガスを供給 する。これによつて、前述したように収容空間 9にバッファ空間 25から外気が流入する ことを防ぐことができ、収容空間 9の酸素濃度を低減することができる。  In the substrate manufacturing apparatus 1 of the present embodiment, the chamber 3 and the buffer chamber 6 are formed symmetrically with respect to the second axis L2, but may not be symmetrical. In this case, the gas supply means 15 adjusts the flow rate of the inert gas flowing from each inert gas inflow hole 16, thereby passing through the communication hole 17 of each buffer chamber 6 to each buffer space 25. The inert gas is supplied to the accommodating space 9 so that the flow rate of the inert gas flowing in is equal. As a result, it is possible to prevent outside air from flowing into the accommodation space 9 from the buffer space 25 as described above, and to reduce the oxygen concentration in the accommodation space 9.

図 7は、本発明の他の実施の形態の基板製造装置 1のバッファ室 6の断面図である 。本実施の形態の基板製造装置 1は、前述の実施の形態の基板製造装置 1とバッフ ァ室 6の構造を除!/、て同様の構成であるので、対応する部分につ!/、ては同一の参照 符号を付して、重複する説明を省略する。  FIG. 7 is a cross-sectional view of the buffer chamber 6 of the substrate manufacturing apparatus 1 according to another embodiment of the present invention. The substrate manufacturing apparatus 1 according to the present embodiment has the same configuration except for the structure of the substrate manufacturing apparatus 1 and the buffer chamber 6 according to the above-described embodiment. Are denoted by the same reference numerals, and redundant description is omitted.

連通管 20は、バッファ室本体 19のチャンバ 3寄りの端部からチャンバ 3に向かって 先細状に延びる。したがって連通孔 17もバッファ空間 25から収容空間 9に近接する にしたがって先細状に形成される。すなわち連通管 20の開口面積がバッファ空間 25 から収容空間 9に近接するにしたがって小さくなるように形成される。  The communication pipe 20 extends in a tapered shape from the end of the buffer chamber body 19 near the chamber 3 toward the chamber 3. Therefore, the communication hole 17 is also formed in a tapered shape as it approaches the accommodating space 9 from the buffer space 25. In other words, the opening area of the communication pipe 20 is formed so as to decrease as it approaches the accommodation space 9 from the buffer space 25.

接続管 22は、バッファ室本体 19の上壁 31から上方 Z1に離間するにしたがって、 上下方向 Zに垂直な断面が広がるように形成される。したがって上下方向 Zに垂直な 排気孔 34の断面の面積、すなわち接続管 22の開口面積がバッファ室本体 19から上 方 Z1に離間するにしたがって大きくなるように形成される。 搬送管 21は、バッファ室本体 19の他側壁 30からチャンバ 3とは反対側に離間する にしたがって、この搬送管 21の延びる方向に垂直な断面が広がるように形成される。 したがって搬送管 21が延びる方向に垂直な搬送孔 23の断面の面積、すなわち搬送 管 21の開口面積がバッファ室本体 19から離間するにしたがって大きくなるように形 成される。 The connection pipe 22 is formed so that a cross section perpendicular to the vertical direction Z increases as the distance from the upper wall 31 of the buffer chamber body 19 increases to the upper Z1. Therefore, the area of the cross section of the exhaust hole 34 perpendicular to the up-down direction Z, that is, the opening area of the connection pipe 22 is formed so as to increase as the distance from the buffer chamber body 19 to the upper side Z1 increases. The transport pipe 21 is formed so that a cross section perpendicular to the extending direction of the transport pipe 21 increases as the distance from the other side wall 30 of the buffer chamber body 19 to the side opposite to the chamber 3 increases. Therefore, the area of the cross section of the transport hole 23 perpendicular to the direction in which the transport pipe 21 extends, that is, the opening area of the transport pipe 21 is formed to increase as the distance from the buffer chamber body 19 increases.

ガスの流路による抵抗は、円管の場合、内径に反比例し、流速の 2乗に比例する。 したがってテーパ形状を有する流路の場合、流路の断面積が小さくなるにしたがって 、内径が小さくなるとともに、流速が大きくなるので、流路による抵抗が大きくなる。す なわち流路の断面積が小さくなる方向よりも流路の断面積が大きくなる方向の方が、 ガスは流れ易い。連通管 20が前述したテーパ形状を有するので、バッファ空間 25か ら連通孔 17を通って収容空間 9にガスが流れるよりも、収容空間 9から連通管 20を通 つてバッファ空間 25にガスが流れ易い。これによつて外気がバッファ室本体 19から 収容空間 9に流入することを防ぐことができ、収容空間 9の酸素濃度を低い値に保つ こと力 Sでさる。  In the case of a circular pipe, the resistance due to the gas flow path is inversely proportional to the inner diameter and proportional to the square of the flow velocity. Accordingly, in the case of a channel having a tapered shape, the inner diameter is reduced and the flow velocity is increased as the cross-sectional area of the channel is reduced, so that the resistance by the channel is increased. That is, gas flows more easily in the direction in which the cross-sectional area of the flow path becomes larger than in the direction in which the cross-sectional area of the flow path decreases. Since the communication pipe 20 has the tapered shape described above, gas flows from the storage space 9 through the communication pipe 20 to the buffer space 25 rather than from the buffer space 25 through the communication hole 17 to the storage space 9. easy. As a result, it is possible to prevent outside air from flowing into the accommodation space 9 from the buffer chamber main body 19, and to maintain the oxygen concentration in the accommodation space 9 at a low value.

また接続管 22が前述したテーパ形状を有するので、排気管 8によって形成される 管路からバッファ空間 25にガスが流入し難くなり、ノ ッファ空間 25から排気した酸素 などを含むガスがバッファ空間 25に逆流することを防ぐことができる。また搬送管 21 が前述したテーパ形状を有するので、外気が搬送孔 23を通ってバッファ空間 25に 流入し難くなる。これらによってバッファ空間 25の酸素濃度を低い値に保つことがで き、ひいては収容空間 9の酸素濃度を低い値に保つことができる。これによつて前述 したように基板 12に不純物が混入することを防ぐことができ、さらに基板製造装置 1の 長寿命化を図ることができる。  Further, since the connecting pipe 22 has the tapered shape described above, it is difficult for gas to flow into the buffer space 25 from the pipe line formed by the exhaust pipe 8, and gas containing oxygen or the like exhausted from the nother space 25 is buffered. Can prevent backflow. Further, since the transfer pipe 21 has the above-described tapered shape, it is difficult for outside air to flow into the buffer space 25 through the transfer hole 23. By these, the oxygen concentration in the buffer space 25 can be kept at a low value, and as a result, the oxygen concentration in the accommodation space 9 can be kept at a low value. As a result, it is possible to prevent impurities from being mixed into the substrate 12 as described above, and to extend the life of the substrate manufacturing apparatus 1.

図 8は、本発明のさらに他の実施の形態の基板製造装置 51を示す断面図である。 本実施の形態の基板製造装置 51は、前述の各実施の形態の基板製造装置 1に加 えて、基板 12の原料 69を補給する補給手段 52をさらに備える。本実施の形態の基 板製造装置 51は、前述の各実施の形態の基板製造装置 1に補給手段 52を加えた 構成なので、対応する部分については同一の符号を付して、補給手段 52について のみ説明し、重複する説明を省略する。なお図 8では、理解の容易のために運搬手 段 5、下地板 4、搬送手段 7およびガス供給手段 15を省略している。 FIG. 8 is a sectional view showing a substrate manufacturing apparatus 51 according to still another embodiment of the present invention. The substrate manufacturing apparatus 51 of the present embodiment further includes a replenishing means 52 that replenishes the raw material 69 of the substrate 12 in addition to the substrate manufacturing apparatus 1 of each of the above-described embodiments. The substrate manufacturing apparatus 51 of the present embodiment has a configuration in which the replenishing means 52 is added to the substrate manufacturing apparatus 1 of each of the above-described embodiments. Only the explanation is omitted, and the duplicate explanation is omitted. In Fig. 8, for ease of understanding, The step 5, the base plate 4, the transfer means 7 and the gas supply means 15 are omitted.

基板製造装置 51は、下地板 4を融液 11に浸漬して融液 11を結晶成長させることに よって基板 12を製造するので、基板 12を製造する毎に基板 12の原料 69となる融液 11が減少していく。補給手段 52は、融液 11が減少すると、この減少分の原料 69を 補うために、固体または液体の金属材料および半導体材料などの原料 69を坩堝 2に 供給する。本実施の形態では補給手段 52は、固体の原料 69を坩堝 2に供給する。 補給手段 52は、チャンバ 3の上方 Z1に設けられる補給用バッファ室 53と、補給用 バッファ室 53からチャンバ 3の上方 Z1の上壁 54に形成される開孔を貫通して収容空 間 9に延びる補給用管 55と、補給用バッファ室 53の上方 Z1の上壁 56から上方 Z1に 延びる補給用搬送管 57と、補給用バッファ室 53の第 2方向 Yの他方の側壁 61から 第 2方向 Yの他方に延びて排気管 8に接続される接続管 62と、補給用バッファ室 53 の第 2方向 Yの一方の側壁 63に配置されるガス噴出手段 64と、補給用搬送管 57に よって形成される管路 (以下、補給用搬送孔という) 65を開閉可能なシャツタを備える 開閉手段とを含んで構成される。  Since the substrate manufacturing apparatus 51 manufactures the substrate 12 by immersing the base plate 4 in the melt 11 and growing the crystal of the melt 11, the melt that becomes the raw material 69 of the substrate 12 every time the substrate 12 is manufactured. 11 will decrease. When the melt 11 decreases, the replenishing means 52 supplies the crucible 2 with a raw material 69 such as a solid or liquid metal material and a semiconductor material in order to supplement the reduced amount of the raw material 69. In the present embodiment, the replenishing means 52 supplies the solid raw material 69 to the crucible 2. The replenishing means 52 passes through the replenishment buffer chamber 53 provided in the upper Z1 of the chamber 3 and the opening formed in the upper wall 54 of the upper Z1 of the chamber 3 from the replenishing buffer chamber 53 to the accommodation space 9. The replenishment pipe 55, the replenishment transfer chamber 57 extending from the upper Z1 upper wall 56 of the replenishment buffer chamber 53, and the replenishment buffer chamber 53 in the second direction Y from the other side wall 61 in the second direction A connection pipe 62 extending to the other side of Y and connected to the exhaust pipe 8, a gas ejection means 64 disposed on one side wall 63 in the second direction Y of the supply buffer chamber 53, and a supply transport pipe 57 And an opening / closing means provided with a shirt capable of opening and closing a formed pipe line (hereinafter referred to as a replenishment conveying hole) 65.

シャツタ 66は、原料 69を坩堝 2に補給するときに補給用搬送孔 65を開状態にし、 それ以外のときに補給用搬送孔 65を閉状態にする。補給用搬送孔 65が開状態にな ると、原料 69が補給用バッファ室 53によって形成されるバッファ空間 68に供給され、 さらに補給用管 55によって形成される管路 70を通って、坩堝 2に供給される。  The shirter 66 opens the supply transport hole 65 when the raw material 69 is supplied to the crucible 2, and closes the supply transport hole 65 at other times. When the replenishment transport hole 65 is opened, the raw material 69 is supplied to the buffer space 68 formed by the replenishment buffer chamber 53, and further passes through the conduit 70 formed by the replenishment pipe 55, and the crucible 2 To be supplied.

ガス噴出手段 64は、前述の各実施の形態のガス噴出手段 35と同様に、接続管 63 によって形成される管路 71に向かって不活性ガスを噴出することによって、ガス噴出 手段 64と接続管 63との間を通過する原料 69に向けて不活性ガスを噴出する。この ようにガス噴出手段 64が不活性ガスを噴出することによって、前述したように外気が 収容空間 9に流入することを防ぐことができ、収容空間 9の酸素濃度を低い値に保つ こと力 Sできる。これによつて、前述したように基板 12に不純物が混入することを防ぐこ とができ、さらに基板製造装置 1の長寿命化を図ることができる。  The gas ejection means 64 is connected to the gas ejection means 64 and the connection pipe by ejecting an inert gas toward the pipe line 71 formed by the connection pipe 63, in the same manner as the gas ejection means 35 of each of the foregoing embodiments. Inert gas is spouted toward the raw material 69 that passes between them. As described above, the gas ejection means 64 ejects the inert gas, so that the outside air can be prevented from flowing into the accommodation space 9, and the oxygen concentration in the accommodation space 9 can be kept at a low value. it can. As a result, it is possible to prevent impurities from being mixed into the substrate 12 as described above, and to further extend the life of the substrate manufacturing apparatus 1.

本実施の形態のさらに他の実施の形態の基板製造装置 51では、前述した基板製 造装置 1の構成に加えて基板 12の破片を回収する回収手段をさらに備える。下地板 4の一表面 4a上に形成される基板 12は、融液 11から離間すると、高温から低温に急 激に冷却されるので、熱応力が発生して破損し、チャンバ 3の下方 Z2の下壁上に破 片が落下する場合がある。回収手段は、チャンバの下壁に落下した基板 12の破片を 再利用するために回収する。 In addition to the configuration of the substrate manufacturing apparatus 1 described above, the substrate manufacturing apparatus 51 according to still another embodiment of the present embodiment further includes a recovery unit that recovers fragments of the substrate 12. When the substrate 12 formed on one surface 4a of the base plate 4 is separated from the melt 11, the substrate 12 suddenly changes from a high temperature to a low temperature. Because it is cooled extremely, thermal stress is generated and it breaks, and there is a possibility that debris falls on the lower wall of Z2 below chamber 3. The collecting means collects the broken pieces of the substrate 12 that have dropped on the lower wall of the chamber for reuse.

回収手段は、基板 12の破片が落下する可能性の高い位置に配置されるトレーと、 基板 12の破片を収容したトレーを収容空間 9から外に運ぶ搬送部とを含んで構成さ れる。チャンバ 3には、回収手段が通過する開口が形成されており、この開口を形成 する開口部に前述した各実施の形態のバッファ室 6と同様の構成のバッファ室 6が接 続される。さらにバッファ空間 25に前述の各実施の形態と同様にガス噴出手段 35が 設けられるとともに、開閉手段 24が設けられる。  The collecting means includes a tray disposed at a position where the fragments of the substrate 12 are highly likely to fall, and a transport unit that carries the trays accommodating the fragments of the substrate 12 out of the accommodation space 9. The chamber 3 is formed with an opening through which the recovery means passes, and the buffer chamber 6 having the same configuration as the buffer chamber 6 of each of the above-described embodiments is connected to the opening forming the opening. Further, in the buffer space 25, the gas jetting means 35 and the opening / closing means 24 are provided as in the above-described embodiments.

前述したようにガス噴出手段 35から噴出される不活性ガスによって、外気が搬送孔 23からバッファ空間 25および連通孔 17を通って収容空間 9に流入することを遮断す る障壁が形成される。これによつて、トレーをバッファ室 6に搬入するまたはバッファ室 6から搬出するときに、外気が収容空間 9に流入することを防ぎ、収容空間 9の酸素 濃度を低レ、値に保つことができる。  As described above, the inert gas ejected from the gas ejection means 35 forms a barrier that blocks the outside air from flowing from the transport hole 23 through the buffer space 25 and the communication hole 17 into the accommodation space 9. This prevents the outside air from flowing into the storage space 9 when the tray is carried into or out of the buffer chamber 6, and the oxygen concentration in the storage space 9 can be kept at a low level. it can.

本発明は、その精神または主要な特徴から逸脱することなぐ他のいろいろな形態 で実施できる。したがって、前述の実施形態はあらゆる点で単なる例示に過ぎず、本 発明の範囲は特許請求の範囲に示すものであって、明細書本文には何ら拘束され ない。さらに、特許請求の範囲に属する変形や変更は全て本発明の範囲内のもので ある。  The present invention can be implemented in various other forms without departing from the spirit or main features thereof. Therefore, the above-described embodiment is merely an example in all respects, and the scope of the present invention is shown in the claims, and is not restricted by the text of the specification. Further, all modifications and changes belonging to the scope of claims are within the scope of the present invention.

産業上の利用可能性 Industrial applicability

本発明によれば、ガス供給手段によって収容空間に不活性ガスが供給される。収 容空間に供給された不活性ガスは、連通孔を通ってバッファ空間に流入し、排気孔 を通ってバッファ空間から排気される。したがって、収容空間に酸素などのガスが流 入したとしても、この不活性ガスの流れに沿って流入したガスを収容空間およびバッ ファ空間から排気することができ、収容空間を不活性ガスによって満たすことができる また開閉手段は、搬送孔を開閉可能なシャツタを備える。このシャツタは、たとえば 搬送孔を冷却体が通過するときに搬送孔を開き、冷却体が搬送孔を通過しないとき には搬送孔を閉じる。これによつて冷却体が搬送孔を通過しないときに、バッファ空 間に空気などの外気が流入することを防ぐことができる。また搬送孔が開いているとき にバッファ空間に空気などの外気が流入したとしても、流入したガスは、収容空間か らバッファ空間を通って排気孔に流れる不活性ガスの流れとともに排気孔から排気さ れるので、収容空間に外気が流入することを防ぐことができる。 According to the present invention, the inert gas is supplied to the accommodation space by the gas supply means. The inert gas supplied to the storage space flows into the buffer space through the communication hole, and is exhausted from the buffer space through the exhaust hole. Therefore, even if a gas such as oxygen flows into the accommodation space, the gas flowing along the flow of the inert gas can be exhausted from the accommodation space and the buffer space, and the accommodation space is filled with the inert gas. The opening / closing means includes a shirter capable of opening and closing the transport hole. For example, this shatter opens the transport hole when the cooling body passes through the transport hole, and does not pass through the transport hole. Close the transport hole. As a result, when the cooling body does not pass through the transport hole, it is possible to prevent outside air such as air from flowing into the buffer space. Even if outside air such as air flows into the buffer space when the transport hole is open, the inflowed gas is exhausted from the exhaust hole along with the flow of inert gas flowing from the containing space through the buffer space to the exhaust hole. Therefore, outside air can be prevented from flowing into the accommodation space.

またガス噴出手段は、バッファ空間において搬送される冷却体に向けて不活性ガス を噴出する。冷却体に不活性ガスを噴出することによって、基板製造装置外からバッ ファ空間に搬入される冷却体とともに移動し、冷却体を覆う酸素などのガスを冷却体 から離間させることができる。このようにして冷却体から離れたガスは、収容空間から バッファ空間を通って排気孔に流れる不活性ガスの流れとともに排気孔力 排気され るので、冷却体を収容空間に搬送するときに外気などが収容空間に流入することを 防ぐこと力 Sできる。このように真空環境用の装置を備えることなぐ簡易な構成で収容 空間に外気が流入することを防いで、収容空間を不活性ガスで満たすことができ、酸 素濃度を低い値に抑えた不活性ガスの雰囲気中において基板を製造することができ る。これによつて融液が凝固成長するときに基板に不純物が混入することを防ぐこと 力 Sできる。さらに収容空間に外気が流入することを防いで収容空間の酸素濃度を低 い値に抑えることができるので、高温となる坩堝などのチャンバに設けられる装置およ びチャンバが酸化して消耗することを防ぐことができ、基板製造装置の長寿命化を図 ること力 Sできる。また真空環境用の装置を備える必要がないので、基板製造装置が複 雑化および大形化して設置面積が大きくなることを防ぎ、基板製造装置のコストを低 く才卬えること力 Sできる。  The gas jetting means jets an inert gas toward the cooling body conveyed in the buffer space. By ejecting the inert gas to the cooling body, the gas moves together with the cooling body carried into the buffer space from the outside of the substrate manufacturing apparatus, and the gas such as oxygen covering the cooling body can be separated from the cooling body. The gas thus separated from the cooling body is exhausted together with the flow of the inert gas flowing from the accommodation space through the buffer space to the exhaust hole, so that when the cooling body is transported to the accommodation space, the outside air or the like is exhausted. Can prevent the flow of water into the containment space. In this way, it is possible to prevent the outside air from flowing into the storage space with a simple configuration without providing a device for a vacuum environment, so that the storage space can be filled with an inert gas, and the oxygen concentration is suppressed to a low value. The substrate can be manufactured in an active gas atmosphere. As a result, it is possible to prevent impurities from entering the substrate when the melt is solidified and grown. Furthermore, since the outside air can be prevented from flowing into the storage space and the oxygen concentration in the storage space can be kept to a low value, the equipment provided in the chamber such as the crucible and the chamber and the chamber are oxidized and consumed. The ability to extend the life of substrate manufacturing equipment can be prevented. In addition, since there is no need to provide a device for a vacuum environment, it is possible to prevent the substrate manufacturing apparatus from becoming complicated and large in size and to increase the installation area, and to reduce the cost of the substrate manufacturing apparatus.

また本発明によれば、ガス供給手段によって各バッファ室の連通孔をそれぞれ等し い流量の不活性ガスが流れる。複数の連通孔のうちの 1または複数の特定の連通孔 を流れる不活性ガスの流量が少な!/、場合、流量の少なレ、連通孔から外気が収容空 間に流入し易くなる力 本発明では各連通孔を流れる不活性ガスの流量がそれぞれ 等しいので、収容空間に外気が流入することを防ぐことができる。これによつて収容空 間の酸素濃度を低減することができ、前述したように基板に不純物が混入することを 防ぐことができ、さらに基板製造装置の長寿命化を図ることができる。 また本発明によれば、バッファ室の容積は、チャンバの容積の 0%を超えてかつ 10 %以下に選ばれる。バッファ空間には、ガス供給手段から供給される不活性ガスが収 容空間から流入するので、バッファ空間の圧力は、少なくとも大気圧よりも高くなる。 バッファ空間の圧力が大気圧より高ければ、搬送孔が開のときに外気がバッファ空間 に流入することを防ぐことができる。バッファ室の容積がチャンバの容積の 10%を超 えて大きい場合には、バッファ空間の圧力が高くなる作用が低下するので、大気圧と バッファ空間の圧力との差が小さくなり、外気がバッファ空間に流入することを防ぐ効 果が小さくなる。本発明のようにバッファ室の容積がチャンバの容積に比べて小さけ れば、バッファ室の容積が大きい場合に比べて、バッファ空間の圧力と大気圧との差 が大きくなり、外気がバッファ室に流入することを効率的に防ぐことができる。これによ つて収容空間の酸素濃度を低減することができ、前述したように基板に不純物が混 入することを防ぐことができ、さらに基板製造装置の長寿命化を図ることができる。 また本発明によれば、ガス噴出手段は、バッファ空間で搬送孔寄りに近接して設け られる。すなわちガス噴出手段は、バッファ空間で連通孔寄りでなぐ搬送孔寄りに おいて冷却体に不活性ガスを噴出する。このように搬送孔から離れた位置において 冷却体を覆う酸素などのガスを離間させるので、離間したガスが搬送孔を通ることを 極力防ぐことができ、外気が収容空間に流れ込むことを防ぐことができる。これによつ て収容空間の酸素濃度を低減することができ、前述したように基板に不純物が混入 することを防ぐことができ、さらに基板製造装置の長寿命化を図ることができる。 また本発明によれば、開閉手段は、搬送孔に近接して設けられるので、開閉手段と 搬送孔との隙間が狭くなる。したがつてこの隙間から空気などのガスが収容空間に流 れ込むことを防ぐことができる。これによつて収容空間の酸素濃度を低減することがで き、前述したように基板に不純物が混入することを防ぐことができ、さらに基板製造装 置の長寿命化を図ることができる。 Further, according to the present invention, the inert gas having the same flow rate flows through the communication hole of each buffer chamber by the gas supply means. If the flow rate of the inert gas flowing through one or more specific communication holes of the plurality of communication holes is small! /, If the flow rate is low, the force that allows outside air to easily flow into the accommodation space from the communication holes. Then, since the flow rate of the inert gas flowing through each communication hole is equal, it is possible to prevent the outside air from flowing into the accommodation space. As a result, the oxygen concentration in the accommodation space can be reduced, impurities can be prevented from being mixed into the substrate as described above, and the life of the substrate manufacturing apparatus can be extended. According to the present invention, the volume of the buffer chamber is selected to be more than 0% and not more than 10% of the chamber volume. Since the inert gas supplied from the gas supply means flows into the buffer space from the storage space, the pressure in the buffer space is at least higher than atmospheric pressure. If the pressure in the buffer space is higher than atmospheric pressure, it is possible to prevent outside air from flowing into the buffer space when the transfer hole is open. When the volume of the buffer chamber is larger than 10% of the volume of the chamber, the effect of increasing the pressure in the buffer space decreases, so the difference between the atmospheric pressure and the pressure in the buffer space decreases, and the outside air flows into the buffer space. The effect of preventing the inflow is reduced. If the volume of the buffer chamber is smaller than the volume of the chamber as in the present invention, the difference between the pressure in the buffer space and the atmospheric pressure becomes larger than when the volume of the buffer chamber is large, and the outside air is Can be efficiently prevented. As a result, the oxygen concentration in the accommodation space can be reduced, as described above, impurities can be prevented from being mixed into the substrate, and the life of the substrate manufacturing apparatus can be extended. According to the invention, the gas jetting means is provided close to the transport hole in the buffer space. That is, the gas jetting means jets an inert gas to the cooling body near the transport hole in the buffer space near the communication hole. Since the gas such as oxygen covering the cooling body is separated at a position away from the transport hole in this way, it is possible to prevent the separated gas from passing through the transport hole as much as possible, and to prevent outside air from flowing into the accommodation space. it can. As a result, the oxygen concentration in the housing space can be reduced, as described above, impurities can be prevented from being mixed into the substrate, and the life of the substrate manufacturing apparatus can be extended. According to the present invention, since the opening / closing means is provided close to the transport hole, the gap between the opening / closing means and the transport hole is narrowed. Therefore, it is possible to prevent gas such as air from flowing into the accommodation space from this gap. As a result, the oxygen concentration in the housing space can be reduced, impurities can be prevented from being mixed into the substrate as described above, and the life of the substrate manufacturing apparatus can be extended.

また本発明によれば、ガス噴出手段は、排気孔に向けて不活性ガスを噴出するの で、ガス噴出手段から排気孔に向力、う不活性ガスの流れが生じる。この不活性ガスの 流れに沿って、不活性ガスを噴出することによって冷却体から離間した酸素などのガ スをスムーズに排気孔に運ぶことができる。これによつて冷却体から離間した酸素な どのガスが連通孔を通って収容空間に流入することを防ぐことができる。これによつて 収容空間の酸素濃度を低減することができ、前述したように基板に不純物が混入す ることを防ぐことができ、さらに基板製造装置の長寿命化を図ることができる。 Further, according to the present invention, since the gas ejection means ejects the inert gas toward the exhaust hole, a flow of inert gas from the gas ejection means to the exhaust hole occurs. By injecting the inert gas along the flow of the inert gas, gas such as oxygen separated from the cooling body can be smoothly conveyed to the exhaust hole. As a result, oxygen away from the cooling body It is possible to prevent any gas from flowing into the accommodation space through the communication hole. As a result, the oxygen concentration in the accommodation space can be reduced, as described above, impurities can be prevented from being mixed into the substrate, and the life of the substrate manufacturing apparatus can be extended.

また本発明によれば、ガス噴出手段は、前記搬送孔を規定する面を延長した仮想 面によって囲まれる領域に、前記領域の外方にわたってガスを噴出する。前記領域 の外方にわたってガスを噴出するので、ガスを噴出する方向に垂直な方向の前記領 域の端部においてガスの流れに乱れが生じず、搬送孔から流入する外気をより効果 的に排気孔に排気することができる。これによつて連通孔を通って収容空間に外気 が流入することを防いで収容空間の酸素濃度を低減することができ、前述したように 基板に不純物が混入することを防ぐことができ、さらに基板製造装置の長寿命化を図 ること力 Sでさる。  Further, according to the present invention, the gas jetting means jets gas over the outside of the region into a region surrounded by a virtual surface extending the surface defining the transport hole. Since the gas is ejected to the outside of the region, the gas flow is not disturbed at the end of the region in the direction perpendicular to the direction in which the gas is ejected, and the outside air flowing from the transfer hole is more effectively exhausted. The holes can be evacuated. As a result, it is possible to reduce the oxygen concentration in the accommodation space by preventing outside air from flowing into the accommodation space through the communication hole, and to prevent impurities from being mixed into the substrate as described above. Use S to extend the life of the board manufacturing equipment.

また本発明によれば、ガス噴出手段は、ガスが噴出する方向に垂直な予め定める 方向に延びて形成され、ガスが噴出する噴出孔を有し、ガスが噴出する方向および 前記予め定める方向に垂直な方向の前記噴出孔の幅の寸法は、 0. 05mm以上か つ 0. 2mm未満に選ばれる。このような寸法に設定することで、不活性ガスの流量を 低く抑えながら、不活性ガスの流速を高くし、し力、も、ガス噴出孔の延びる方向におけ る不活性ガスの流速を均一にすることができる。  According to the invention, the gas ejection means is formed to extend in a predetermined direction perpendicular to the direction in which the gas is ejected, and has an ejection hole through which the gas is ejected, and in the direction in which the gas is ejected and the predetermined direction. The width dimension of the jet hole in the vertical direction is selected to be not less than 0.05 mm and less than 0.2 mm. By setting such dimensions, the flow rate of the inert gas is increased while the flow rate of the inert gas is kept low, and the flow rate of the inert gas in the direction in which the gas ejection holes extend is uniform. Can be.

また本発明によれば、ガス噴出手段から噴出される不活性ガスは、希ガスおよび窒 素ガスの少なくともいずれか一方に選ばれる。ガス噴出手段は、このような不活性ガ スを噴出するので、ガス噴出手段から噴出された不活性ガスが連通孔を通って収容 空間に流入したとしても、基板に不純物が混入することがなぐまた高温となる坩堝な どのチャンバに設けられる装置およびチャンバがガス噴出手段から噴出される不活 性ガスと反応して消耗することがない。これによつて前述したように基板に不純物が 混入することを防ぐことができ、さらに基板製造装置の長寿命化を図ることができる。 また、本発明によれば、ガス噴出手段は、原料を凝固成長させる冷却体の表面に 対して平行な方向に、不活性ガスを噴出する。したがって、冷却体が板状で、その面 積最大の表面に基板を形成する場合でも、冷却体が不活性ガスの流れを乱し難ぐ また、基板を形成する表面とこの表面に対向する表面とに不活性ガスが均等に噴射 されて、これら両表面を覆って搬送される外気が速やかにかつ確実に排除される。 According to the invention, the inert gas ejected from the gas ejection means is selected as at least one of a rare gas and a nitrogen gas. Since the gas ejection means ejects such an inert gas, even if the inert gas ejected from the gas ejection means flows into the accommodation space through the communication hole, impurities are not mixed into the substrate. Further, the apparatus provided in the chamber such as a crucible at a high temperature and the chamber do not react with the inert gas ejected from the gas ejection means and are not consumed. As a result, as described above, impurities can be prevented from being mixed into the substrate, and the life of the substrate manufacturing apparatus can be extended. Further, according to the present invention, the gas ejection means ejects the inert gas in a direction parallel to the surface of the cooling body for solidifying and growing the raw material. Therefore, even when the cooling body is plate-shaped and the substrate is formed on the surface having the largest surface area, the cooling body hardly disturbs the flow of the inert gas. Also, the surface that forms the substrate and the surface that faces this surface Inert gas is sprayed evenly Thus, the outside air that is transported covering both surfaces is quickly and reliably eliminated.

Claims

請求の範囲 The scope of the claims [1] 基板の原料を加熱溶融した融液に冷却体を浸漬し、前記冷却体の表面上に前記 原料を凝固成長させて基板を製造する基板製造装置であって、  [1] A substrate manufacturing apparatus for manufacturing a substrate by immersing a cooling body in a melt obtained by heating and melting a raw material of a substrate, and solidifying and growing the raw material on the surface of the cooling body, 前記融液を貯留する坩堝を備え、前記坩堝が収容される収容空間を形成するチヤ ンバと、  A chamber comprising a crucible for storing the melt, and forming a chamber for accommodating the crucible; 前記収容空間に不活性ガスを供給するガス供給手段と、  Gas supply means for supplying an inert gas to the accommodation space; 前記収容空間に連通し、かつ冷却体が通過可能な連通孔、ガスが排気される排気 孔、および外部空間に連なり、かつ冷却体が通過可能な搬送孔が形成され、前記連 通孔、排気孔および搬送孔に連通するバッファ空間を形成するバッファ室と、 前記搬送孔を開閉可能なシャツタを備える開閉手段と、  A communication hole that communicates with the housing space and allows the cooling body to pass therethrough, an exhaust hole that exhausts gas, and a transport hole that communicates with the external space and allows the cooling body to pass therethrough are formed. A buffer chamber that forms a buffer space communicating with the hole and the transport hole; and an opening / closing means that includes a shirter capable of opening and closing the transport hole; 前記連通孔および搬送孔を通って、収容空間に冷却体を搬入し、かつ収容空間か ら冷却体を搬出する搬送手段と、  A conveying means for carrying the cooling body into the accommodation space through the communication hole and the conveyance hole and carrying out the cooling body from the accommodation space; バッファ空間に収容され、搬送手段によってバッファ空間を搬送される冷却体に向 けて不活性ガスを噴出するガス噴出手段とを含むことを特徴とする基板製造装置。  A substrate manufacturing apparatus comprising: a gas ejection unit that ejects an inert gas toward a cooling body that is accommodated in the buffer space and is conveyed through the buffer space by the conveyance unit. [2] 複数の前記バッファ室を有し、  [2] having a plurality of the buffer chambers; 前記ガス供給手段は、各バッファ室の連通孔を通って各バッファ空間にそれぞれ 流入する不活性ガスの流量が等しくなるように前記収容空間に不活性ガスを供給す ることを特徴とする請求項 1記載の基板製造装置。  The gas supply means supplies the inert gas to the accommodation space so that the flow rates of the inert gas flowing into the buffer spaces through the communication holes of the buffer chambers are equal to each other. The board manufacturing apparatus according to 1. [3] 前記バッファ室の容積は、前記チャンバの容積の 0%を超えてかつ 10%以下に選 ばれることを特徴とする請求項 1または 2記載の基板製造装置。 3. The substrate manufacturing apparatus according to claim 1, wherein the volume of the buffer chamber is selected to be greater than 0% and less than or equal to 10% of the volume of the chamber. [4] 前記ガス噴出手段は、バッファ空間で搬送孔寄りに近接して設けられることを特徴 とする請求項;!〜 3のいずれか 1つに記載の基板製造装置。 [4] The substrate manufacturing apparatus according to any one of [1] to [3], wherein the gas ejection means is provided in the buffer space in the vicinity of the transport hole. [5] 前記開閉手段は、前記搬送孔に近接して設けられることを特徴とする請求項;!〜 4 のいずれか 1つに記載の基板製造装置。 [5] The substrate manufacturing apparatus according to any one of [1] to [4], wherein the opening / closing means is provided in the vicinity of the transport hole. [6] 前記ガス噴出手段は、排気孔に向けて不活性ガスを噴出することを特徴とする請 求項 1〜5のいずれ力、 1つに記載の基板製造装置。 [6] The substrate manufacturing apparatus according to any one of claims 1 to 5, wherein the gas jetting means jets an inert gas toward the exhaust hole. [7] 前記ガス噴出手段は、前記搬送孔を規定する面を延長した仮想面によって囲まれ る領域に、前記領域の外方にわたってガスを噴出することを特徴とする請求項 6記載 の基板製造装置。 [7] The gas jetting means jets a gas to the outside of the region in a region surrounded by a virtual surface extending the surface defining the transport hole. Board manufacturing equipment. [8] 前記ガス噴出手段は、不活性ガスが噴出する方向に垂直な予め定める方向に延 びて形成され、不活性ガスが噴出する噴出孔を有し、  [8] The gas ejection means is formed to extend in a predetermined direction perpendicular to the direction in which the inert gas is ejected, and has an ejection hole through which the inert gas is ejected. ガスが噴出する方向および前記予め定める方向に垂直な方向の前記噴出孔の幅 の寸法は、 0. 05mm以上かつ 0. 2mm未満に選ばれることを特徴とする請求項 1〜 The dimension of the width of the ejection hole in the gas ejection direction and the direction perpendicular to the predetermined direction is selected to be not less than 0.05 mm and less than 0.2 mm. 7のいずれか 1つに記載の基板製造装置。 8. The board manufacturing apparatus according to any one of 7. [9] 前記ガス噴出手段から噴出される不活性ガスは、希ガスおよび窒素ガスのうちの少 なくともいずれか一方に選ばれることを特徴とする請求項 1〜8のいずれ力、 1つに記 載の基板製造装置。 [9] The force according to any one of claims 1 to 8, wherein the inert gas ejected from the gas ejection means is selected as at least one of a rare gas and a nitrogen gas. The substrate manufacturing apparatus described above. [10] 前記ガス噴出手段は、前記原料を凝固成長させる前記冷却体の表面に対して平 行な方向に、不活性ガスを噴出することを特徴とする請求項 1〜9のいずれか 1つに 記載の基板製造装置。  [10] The gas jetting means jets an inert gas in a direction parallel to a surface of the cooling body that solidifies and grows the raw material. The board | substrate manufacturing apparatus of description.
PCT/JP2007/067767 2006-09-12 2007-09-12 Substrate production equipment Ceased WO2008032752A1 (en)

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JP2001049432A (en) * 1999-08-02 2001-02-20 Sony Corp Work movable reactive sputtering apparatus and work movable reactive sputtering method
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