WO2023143297A1 - Device and method for manufacturing silicon carbide polycrystal - Google Patents

Device and method for manufacturing silicon carbide polycrystal Download PDF

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Publication number
WO2023143297A1
WO2023143297A1 PCT/CN2023/072842 CN2023072842W WO2023143297A1 WO 2023143297 A1 WO2023143297 A1 WO 2023143297A1 CN 2023072842 W CN2023072842 W CN 2023072842W WO 2023143297 A1 WO2023143297 A1 WO 2023143297A1
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WO
WIPO (PCT)
Prior art keywords
silicon carbide
graphite
crucible
holder
polycrystalline
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PCT/CN2023/072842
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French (fr)
Chinese (zh)
Inventor
郭超
母凤文
Original Assignee
北京青禾晶元半导体科技有限责任公司
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Publication of WO2023143297A1 publication Critical patent/WO2023143297A1/en

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    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B29/00Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
    • C30B29/10Inorganic compounds or compositions
    • C30B29/36Carbides
    • 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
    • C30B28/00Production of homogeneous polycrystalline material with defined structure
    • C30B28/04Production of homogeneous polycrystalline material with defined structure from liquids

Definitions

  • the present application relates to the technical field of semiconductor manufacturing, for example, to a silicon carbide polycrystalline manufacturing device and method.
  • Silicon carbide is a wide bandgap semiconductor material. Devices made of silicon carbide substrates have the advantages of high temperature resistance, high voltage resistance, high frequency, high power, radiation resistance, and high efficiency. They are important in the fields of radio frequency and new energy vehicles. application value.
  • Silicon carbide includes silicon carbide single crystal and silicon carbide polycrystal.
  • the present application provides a silicon carbide polycrystalline manufacturing device and method.
  • the present application provides a silicon carbide polycrystalline manufacturing device, including:
  • an induction coil is arranged in the chamber
  • a graphite crucible is arranged in the chamber, and the graphite crucible is used for accommodating a cosolvent, and the inner wall of the bottom of the graphite crucible can grow polycrystalline silicon carbide;
  • a crystal rod one end of the crystal rod is located in the graphite crucible, and the other end of the crystal rod is located outside the chamber;
  • the graphite support is fixedly connected to one end of the crystal rod, and the bottom surface of the graphite support facing the bottom wall of the graphite crucible can grow polycrystalline silicon carbide.
  • the present application provides a silicon carbide polycrystalline manufacturing method, which is applied to the above-mentioned silicon carbide polycrystalline manufacturing device, including:
  • FIG. 1 is a schematic structural view of a silicon carbide polycrystalline manufacturing device provided in Embodiment 1 of the present application;
  • Fig. 2 is the schematic diagram of the assembly of the graphite crucible, the crystal rod and the graphite holder provided in the first embodiment of the present application;
  • Fig. 3 is a reference diagram of the use state of the graphite crucible, the crystal rod and the graphite support provided in the first embodiment of the present application;
  • Fig. 4 is a schematic structural view of a crystal rod and a graphite holder provided in Embodiment 1 of the present application;
  • Fig. 5 is a top view of the crystal rod provided in Embodiment 1 of the present application.
  • Fig. 6 is a schematic structural view of a crucible holder and a graphite crucible provided in Embodiment 1 of the present application;
  • FIG. 7 is a flowchart of a method for manufacturing a silicon carbide polycrystal provided in Embodiment 2 of the present application.
  • Silicon carbide includes silicon carbide single crystal and silicon carbide polycrystal.
  • a solution method is used to grow silicon carbide single crystal.
  • the basic principle of the solution method is: put a silicon-containing flux in a graphite crucible and melt it by induction heating Flux, the carbon in the graphite crucible is dissolved in the flux; then the silicon carbide seed crystal is placed on the liquid level of the flux, and due to the supercooling of the seed crystal, carbon is precipitated on the solid-liquid interface of the seed crystal, and with the flux
  • the silicon in the flux combines to form a single crystal of silicon carbide.
  • embodiments of the present application provide a silicon carbide polycrystalline manufacturing device and method.
  • connection should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integrated ; It can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediary, and it can be the internal communication of two components or the interaction relationship between two components.
  • connection can be a fixed connection, a detachable connection, or an integrated ; It can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediary, and it can be the internal communication of two components or the interaction relationship between two components.
  • the first feature is “on” the second feature
  • “under” may include that the first and second features are in direct contact, and may also include that the first and second features are not in direct contact but are in contact through another feature therebetween.
  • “above”, “above” and “above” the first feature on the second feature include that the first feature is directly above and obliquely above the second feature, or simply means that the first feature is horizontally higher than the second feature.
  • “Below”, “beneath” and “under” the first feature to the second feature include that the first feature is directly below and obliquely below the second feature, or simply means that the first feature has a lower level than the second feature.
  • This embodiment provides a silicon carbide polycrystalline manufacturing device, which can be used to grow and manufacture silicon carbide polycrystalline, and has higher efficiency and lower cost.
  • a silicon carbide polycrystalline manufacturing device includes a chamber 1 , an induction coil 2 , a graphite crucible 3 , a crystal rod 4 and a graphite holder 5 .
  • the cavity 1 is used to provide a relatively sealed space for the growth of polycrystalline silicon carbide, and the cavity 1 has at least one gas extraction port, through which the cavity 1 can be evacuated.
  • the pumping port is connected to a vacuum device, so that the vacuum device can pump the chamber 1 through the pumping port, so as to reduce the air pressure in the chamber 1 to a required value.
  • the chamber 1 is also connected with at least one vacuum gauge, and the vacuum gauge is used to measure the pressure in the chamber 1 .
  • the chamber 1 also has at least one gas filling port, through which nitrogen, argon, helium or other inert gases can be filled into the chamber 1, so that the silicon carbide polycrystalline grow.
  • the induction coil 2 and the graphite crucible 3 are respectively arranged in the chamber 1, and the graphite crucible 3 is used for accommodating a cosolvent. As shown in FIG. 2 , the induction coil 2 is used to inductively heat the co-solvent 100 in the graphite crucible 3 to melt the co-solvent 100 in the graphite crucible 3 . In some embodiments, the induction coil 2 has multiple turns, which are arranged at intervals around the graphite crucible 3 to achieve uniform heating.
  • the current frequency of the induction coil 2 is 1-100kHz, and the induction coil 2 is hollow and can be cooled by water.
  • One end of the crystal rod 4 is located in the graphite crucible 3, the other end of the crystal rod 4 is located outside the chamber 1, and the graphite holder 5 is fixedly connected to one end of the crystal rod 4 and is located in the graphite crucible 3, and the crystal rod 4 can drive the graphite holder 5 to be opposite to each other.
  • the graphite crucible 3 moves, such as driving the graphite holder 5 to rotate or move along the up and down direction in FIG. 1 .
  • the other end of the crystal rod 4 is connected with a driving member, and the driving member can provide driving force to the crystal rod 4 .
  • Both the bottom surface of the graphite holder 5 facing the bottom wall of the graphite crucible 3 and the bottom inner wall of the graphite crucible 3 can grow silicon carbide polycrystals, so that multiple pieces of silicon carbide polycrystals can be obtained in one process.
  • the silicon carbide polycrystalline manufacturing device provided in this embodiment can adopt the solution method to manufacture silicon carbide polycrystalline.
  • the seed crystal is set, and the graphite holder 5 and the graphite crucible 3 can be crystallized at the same time, so that one device can obtain two silicon carbide polycrystals at the same time, which improves the manufacturing efficiency of silicon carbide polycrystals and reduces the cost of manufacturing silicon carbide polycrystals.
  • the inner wall of the bottom of the graphite crucible 3 is fixed with a carbon film layer 6, the setting of the carbon film layer 6 can reduce the stress of the crystallization process, and avoid the occurrence of cracks in the grown silicon carbide polycrystalline At the same time, it can also facilitate the separation of the silicon carbide polycrystal and the graphite crucible 3, avoid destructive separation due to too strong bonding between the silicon carbide polycrystal and the graphite crucible 3, and ensure the quality of the silicon carbide polycrystal. It should be noted that the carbon film layer 6 can completely cover the bottom inner wall of the graphite crucible 3 to ensure the growth uniformity and growth area of the silicon carbide polycrystal.
  • the bottom surface of the graphite holder 5 has a carbon film layer 6.
  • the carbon film layer 6 can facilitate the separation between the silicon carbide polycrystal and the graphite holder 5, ensuring the stability of the silicon carbide polycrystal grown on the graphite holder 5. quality. It should be noted that the carbon film layer 6 can completely cover the bottom surface of the graphite support 5 to ensure the growth uniformity and growth area of the silicon carbide polycrystal.
  • the carbon film layer 6 can be prepared by chemical vapor deposition, and can also be deposited by physical vapor deposition, magnetron sputtering, electron beam evaporation, high-temperature curing after coating graphite glue or sugar glue, etc. This embodiment does not limit it.
  • blocky silicon carbide polycrystal 10 can be obtained under the carbon film layer 6 on the bottom surface of the graphite holder 5, and block can be obtained on the carbon film layer 6 at the bottom of the graphite crucible 3 SiC polycrystalline 10.
  • the bottom surface of the graphite crucible 3 is connected with the silicon carbide polycrystal 10 through the carbon film layer 6, and the sidewall of the silicon carbide polycrystal 10 and the graphite crucible 3 may be bonded, that is, the silicon carbide polycrystal 10 appears sticking to the pot and grows.
  • a carbon film layer 6 of a certain height can be plated on the sidewall of the graphite crucible 3, so that the carbon in the graphite crucible 3 is dissolved in the cosolvent 100 without hindering it.
  • the polycrystalline silicon carbide 10 and the graphite crucible 3 can be separated better.
  • the silicon carbide polycrystalline manufacturing device is cooled, the silicon carbide polycrystalline 10 can be separated from the carbon film layer 6 on the graphite support 5 , and the silicon carbide polycrystalline 10 can be separated from the carbon film layer 6 at the bottom of the graphite crucible 3 .
  • the thickness of the carbon film layer 6 in this embodiment is 1-1000 microns, for example, the thickness of the carbon film layer 6 is 10-100 microns.
  • the crystal rod 4 has a first cooling channel 41 , and the cooling fluid in the first cooling channel 41 is used to cool the graphite holder 5 . Due to the need for supercooling at the graphite support 5 during the formation of silicon carbide polycrystals, the carbon in the co-solvent 100 is precipitated on the solid-liquid interface between the graphite support 5 and the co-solvent 100, and combines with the silicon in the co-solvent Silicon carbide polycrystalline is formed, therefore, in order to ensure that the graphite support 5 has the required supercooling, a first cooling flow channel 41 can be set on the crystal rod 4, and the heat on the graphite support 5 can be taken away by the first cooling flow channel 41 , so that the graphite support 5 is in a supercooled state. In some embodiments, the first cooling channel 41 is connected to one end of the graphite support 5 through the crystal rod 4 to better cool the graphite support 5 .
  • the cooling fluid flowing in the first cooling channel 41 can be helium.
  • the flow rate of helium in the first cooling channel 41 can be controlled, thereby controlling the temperature near the graphite support 5 Gradient, so as to control the growth rate and quality of silicon carbide polycrystals on the graphite support 5, so that the obtained silicon carbide polycrystals meet the requirements.
  • the crystal rod 4 includes a first tube body 42 and a second tube body 43 sleeved outside the first tube body 42.
  • the first tube body 42 is suspended in the air. in the second pipe body 43 .
  • One end of the second tube body 43 is fixedly connected to the graphite holder 5 , and the other end of the second tube body 43 extends out of the chamber 1 .
  • the first cooling channel 41 includes a first sub-channel 411 formed by the first tube body 42 and a second sub-channel 412 formed by the gap between the first tube body 42 and the second tube body 43.
  • the flow channel 411 communicates with the second sub-channel 412, so that the cooling fluid can flow from the first sub-channel 411 into the second sub-channel 412 or from the second sub-channel 412 into the first sub-channel 411, thereby forming a loop .
  • the first end of the first tube body 42 close to the end of the second tube body 43 is an open end, and the first end of the first tube body 42 is spaced apart from one end of the second tube body 43, so that the first The cooling fluid in the pipe body 42 can flow out from the first end of the first pipe body 42 and enter between the first pipe body 42 and the second pipe body 43.
  • One end of the second pipe body 43 is a sealed end or an open end.
  • the second pipe body 43 When one end of the second pipe body 43 is an open end, the second pipe body 43 is sealed and connected with the graphite holder 5 .
  • the first end of the first tube body 42 close to the end of the second tube body 43 is a sealed end.
  • the first end of the first pipe body 42 is provided with a through hole, and the cooling fluid in the first pipe body 42 can flow into the space between the first pipe body 42 and the second pipe body 43 through the through hole.
  • first tube body 42 and the second tube body 43 can move relative to each other.
  • the second tube body 43 can be directly driven to rotate, while the first tube body 42 remains stationary. .
  • the end surface of the second end of the first tube body 42 away from the end of the second tube body 43 can be flush with the end surface of the second tube body 43, that is, the end surface of the end surface of the crystal rod 4 not connected to the graphite holder 5
  • the first cooling channel 41 has a cooling inlet 413 and a cooling outlet 414 located at the end surface of the crystal rod 4, and the cooling channel can flow into the first cooling channel 41 through the cooling inlet 413, for example, into the first cooling channel 41.
  • a sub-channel 411 and flows to the vicinity of the graphite holder 5 , absorbs the heat of the graphite holder 5 , passes through the second sub-channel 412 and flows out from the cooling outlet 414 .
  • the cooling inlet 413 in this embodiment is a central hole
  • the cooling outlet 414 is an annular hole arranged around the cooling inlet 413 .
  • the end surface of the crystal rod 4 not connected to the graphite holder 5 may not be a plane, that is, the length of the first tube body 42 is greater than the length of the second tube body 43 .
  • the first cooling channel 41 may be connected to a driving pump, and the driving pump provides driving force for the helium in the first cooling channel 41.
  • the crystal rod 4 includes a first tube body 42
  • the first tube Body 42 is connected to the drive pump.
  • the silicon carbide polycrystalline manufacturing device also includes a crucible holder 7 .
  • one end of the crucible holder 7 is fixedly connected to the bottom wall of the graphite crucible 3 , and the other end of the crucible holder 7 is located outside the chamber 1 .
  • the crucible holder 7 can drive the graphite crucible 3 to rotate.
  • the crucible holder 7 can rotate under the drive of the driving mechanism, thereby driving the graphite crucible to rotate.
  • the crucible holder 7 can also drive the graphite crucible 3 to move in the up and down direction shown in FIG.
  • the rotation direction of the crucible holder 7 is opposite to the rotation direction of the crystal rod 4; in other embodiments, the rotation speed of the crucible holder 7 or the crystal rod 4 may also be periodically changed or rotated forward periodically and reverse.
  • the crucible holder 7 has a second cooling channel 71 , and the cooling fluid in the second cooling channel 71 is used to cool the bottom wall of the graphite crucible 3 .
  • the carbon in the co-solvent 100 is precipitated on the solid-liquid interface between the graphite crucible 3 and the co-solvent 100, and combines with the silicon in the co-solvent Form silicon carbide polycrystal, therefore, in order to ensure that the graphite crucible 3 place has the required supercooling, a second cooling flow channel 71 can be set on the crucible holder 7, and the heat on the graphite crucible 3 can be taken away by the second cooling flow channel 71 , so that the graphite crucible 3 is in a supercooled state.
  • the second cooling channel 71 is connected to one end of the graphite crucible 3
  • the cooling fluid flowing in the second cooling channel 71 can be helium
  • the flow rate of helium in the second cooling channel 71 can be controlled, and then the temperature near the graphite crucible 3 can be controlled Gradient, so as to realize the control of the growth rate and quality of the silicon carbide polycrystal on the graphite crucible 3, so that the obtained silicon carbide polycrystal meets the requirements.
  • the crucible holder 7 includes a third tube body 72 and a fourth tube body 73 sleeved outside the third tube body 72.
  • the third tube body 72 is suspended in the air. in the fourth tube body 73 .
  • One end of the fourth tube body 73 is fixedly connected to the graphite crucible 3 , and the other end of the fourth tube body 73 extends out of the chamber 1 .
  • the second cooling channel 71 includes a third sub-channel 711 formed by the third tube body 72 and a fourth sub-channel 712 formed by the gap between the third tube body 72 and the fourth tube body 73.
  • the runner 711 is connected with the fourth sub-runner 712 so that the cooling fluid can flow from the third sub-channel 711 into the fourth sub-channel 712 or from the fourth sub-channel 712 into the third sub-channel 711, thereby forming a loop.
  • the third end of the third pipe body 72 close to the end of the fourth pipe body 73 is an open end, and the third end of the third pipe body 72 is spaced from the end of the fourth pipe body 73, so that the third The cooling fluid in the pipe body 72 can flow out from the third end of the third pipe body 72 and enter between the third pipe body 72 and the fourth pipe body 73.
  • One end of the fourth pipe body 73 is a sealed end or an open end.
  • the fourth pipe body 73 When one end of the fourth pipe body 73 is an open end, the fourth pipe body 73 is in sealing connection with the graphite crucible 3 .
  • the third end of the third tube body 72 close to the end of the fourth tube body 73 is a sealed end.
  • the pipe wall at the third end of the third pipe body 72 is provided with a through hole, and the cooling fluid in the third pipe body 72 can flow into the third pipe body 72 and the fourth pipe body 73 through the through hole on the third pipe body 72 between.
  • the third pipe body 72 and the fourth pipe body 73 can move relative to each other.
  • the fourth pipe body 73 can be directly driven to rotate, while the third pipe body 72 remains stationary .
  • the end face of the fourth end of the third pipe body 72 away from the end of the fourth pipe body 73 can be flush with the end face of the fourth pipe body 73, that is, the end face of the end face of the crucible holder 7 that is not connected to the graphite crucible 3 It is a plane, please continue to refer to FIG.
  • the second cooling channel 71 has an inlet 713 and an outlet 714 on the end surface of the crucible holder 7, the cooling channel can flow into the second cooling channel 71 through the inlet 713, for example, into the third sub- flow channel 711 , and flow to the vicinity of the graphite crucible 3 , absorb the heat of the graphite crucible 3 , pass through the fourth sub-channel 712 and flow out from the outlet 714 .
  • the inlet 713 is a central hole
  • the outlet 714 is an annular hole arranged around the inlet 713 .
  • the end surface of the crucible holder 7 not connected to the end of the graphite crucible 3 may not be a plane, that is, the length of the third tube body 72 is greater than the length of the fourth tube body 73 .
  • the second cooling channel 71 may be connected to a driving pump, and the driving pump provides driving force for the helium in the second cooling channel 71.
  • the crucible holder 7 includes a third tube body 72, the third tube Body 72 is connected to the drive pump.
  • the silicon carbide polycrystalline manufacturing device also includes a heat insulating cover 8, the graphite crucible 3 is arranged in the heat insulating cover 8, the induction coil 2 is located outside the heat insulating cover 8, and the crucible holder 7 and the crystal rod 4 respectively pass through the heat insulating cover 8.
  • the heat insulation sleeve 8 is made of heat insulation material, and is used for heat insulation of the graphite crucible 3.
  • the silicon carbide polycrystal manufacturing device provided in this embodiment can form two silicon carbide polycrystals in one manufacturing process, which improves the manufacturing efficiency of the silicon carbide polycrystal and has a lower cost.
  • This embodiment provides a silicon carbide polycrystalline manufacturing method, which is applied to the silicon carbide polycrystalline manufacturing device in Embodiment 1. As shown in FIG. 7, the silicon carbide polycrystalline manufacturing method includes the following steps:
  • the co-solvent 100 in this embodiment is a co-solvent containing silicon, so that silicon in the co-solvent 100 can form silicon carbide polycrystals with carbon. It can be understood that, in addition to silicon, the co-solvent 100 can also include titanium Ti, chromium Cr, scandium Sc, nickel Ni, aluminum Al, cobalt Co, manganese Mn, magnesium Mg, germanium Ge, arsenic As, boron P, nitrogen One or more elements of N, oxygen O, boron B, dysprosium Dy, yttrium Y, niobium Nb, neodymium Nd, and iron Fe.
  • step S2 the induction coil 2 is energized to heat the induction coil 2 and melt the co-solvent 100, so that the co-solvent 100 is in a liquid state.
  • the fact that the lower surface of the graphite support 5 is flush with the liquid surface of the co-solvent 100 means that the lower surface of the graphite support 5 is just in contact with the liquid surface of the co-solvent 100 .
  • the preset spacing is up to 5mm to ensure the smooth growth of SiC polycrystalline. It should be noted that, when the lower surface of the graphite support 5 is provided with the carbon film layer 6, the lower surface of the carbon film layer 6 is controlled to be flush with the liquid level of the co-solvent 100 or the distance is smaller than the preset distance.
  • both the lower surface of the graphite holder 5 and the inner wall at the bottom of the graphite crucible 3 can grow polycrystalline silicon carbide.
  • the silicon carbide polycrystalline manufacturing device includes a crucible holder 7, and the crucible body 7 has a second cooling flow channel 71, and the crystal rod 4 has a first cooling flow channel 41, in step S4, simultaneously The flow rate of the cooling fluid in the first cooling channel 41 and the second cooling channel 71 is controlled, thereby controlling the temperature gradient near the graphite support 5 and the graphite crucible 3 , and then controlling the growth rate and quality of the silicon carbide polycrystal.
  • the silicon carbide polycrystalline manufacturing method provided in this embodiment can adopt the solution method to manufacture silicon carbide polycrystalline, and by setting the graphite support 5 and the graphite crucible 3, it can realize direct crystallization on the graphite material, and then obtain the silicon carbide polycrystalline, without The seed crystal is set, and the graphite holder 5 and the graphite crucible 3 can be crystallized at the same time, so that one device can obtain two silicon carbide polycrystals at the same time, which improves the manufacturing efficiency of silicon carbide polycrystals and reduces the cost of manufacturing silicon carbide polycrystals.
  • the p-type silicon carbide polycrystal and the n-type silicon carbide polycrystal can be obtained by controlling the growth environment of the silicon carbide polycrystal and the parameters of the cosolvent 100 .
  • the bottom inner wall of the graphite crucible 3 and the bottom surface of the graphite holder 5 have a carbon film layer 6 respectively
  • the above-mentioned silicon carbide polycrystal manufacturing method also includes filling helium into the chamber ,
  • the gas pressure in the chamber 1 is 0.5-1 atmosphere, and the co-solvent 100 is adjusted to include Si, Cr and Al elements, and the temperature of the co-solvent 100 is controlled to 1800° C. through the induction coil 2 .
  • step S4 the crystal rod 4 is controlled to drive the graphite holder 5 to move away from the cosolvent while driving the graphite holder 5 to rotate, for example, the pulling speed of the crystal rod 4 is 1-2 mm/hour, and the graphite crucible 3 is controlled to reversely Rotate in the direction of the rotation direction of the graphite holder 5 to simultaneously crystallize on the carbon film layer 6 below the graphite holder 5 and on the carbon film layer 6 on the bottom wall of the graphite crucible 3 to obtain two p-type silicon carbide polycrystals.
  • the resistivity of the p-type silicon carbide polycrystalline obtained in this embodiment is lower than 30 m ⁇ cm (milliohm ⁇ cm).
  • the manufacture method of silicon carbide polycrystal also comprises filling helium in chamber 1 and nitrogen.
  • nitrogen gas is filled into the chamber 1 at a fixed flow rate, and the main growth atmosphere of silicon carbide polycrystalline is helium gas.
  • the pressure of the gas in the chamber 1 is controlled to be 0.5-1 atmosphere, the co-solvent includes Si element and Cr element, and the temperature of the co-solvent is 2000°C.
  • step S4 the crystal rod 4 is controlled to drive the graphite holder 5 to move away from the cosolvent while driving the graphite holder 5 to rotate, for example, the pulling speed of the crystal rod 4 is 1-2 mm/hour, and the graphite crucible 3 is controlled to reversely Rotate in the direction of the rotation direction of the graphite holder 5 to simultaneously crystallize on the carbon film layer 6 below the graphite holder 5 and on the carbon film layer 6 on the bottom wall of the graphite crucible 3 to obtain two n-type silicon carbide polycrystals.
  • the n-type silicon carbide polycrystalline resistivity obtained in this embodiment is lower than 30 m ⁇ cm (milliohm ⁇ cm).
  • one process parameter is the flow rate of the cooling helium in the crystal rod 4 and the crucible holder 7 .
  • a process parameter is growth atmosphere and pressure.
  • the growth atmosphere is at least one of helium, argon, nitrogen, and hydrogen, and the pressure is between 0.2-2 atmospheres.
  • One process parameter is the rotation speed of the crystal rod 4 , the upward pulling speed, and the rotation speed of the graphite crucible 3 .
  • One process parameter is the power of the induction heating to control the temperature of the flux 100 .

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  • Crystallography & Structural Chemistry (AREA)
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  • Inorganic Chemistry (AREA)
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Abstract

A device and method for manufacturing a silicon carbide polycrystal. The device for manufacturing a silicon carbide polycrystal comprises a chamber (1), an induction coil (2), a graphite crucible (3), a crystal rod (4), and a graphite support (5), wherein the induction coil (2) is arranged inside the chamber (1), the graphite crucible (3) is arranged inside the chamber (1), the graphite crucible (3) is configured for containing a cosolvent, and an inner wall of the bottom of the graphite crucible (3) can be configured for silicon carbide polycrystal growth; one end of the crystal rod (4) is positioned in the graphite crucible (3), and the other end of the crystal rod (4) is positioned outside the chamber (1); and the graphite support (5) is fixedly connected to one end of the crystal rod (4), and the bottom surface of the graphite support (5) facing a bottom wall of the graphite crucible (3) can be configured for silicon carbide polycrystal growth.

Description

碳化硅多晶的制造装置及方法Device and method for manufacturing silicon carbide polycrystalline
本申请要求在2022年01月29日提交中国专利局、申请号为202210112585.0的中国专利申请的优先权,以上申请的全部内容通过引用结合在本申请中。This application claims the priority of the Chinese patent application with application number 202210112585.0 submitted to the China Patent Office on January 29, 2022, and the entire content of the above application is incorporated in this application by reference.
技术领域technical field
本申请涉及半导体制造技术领域,例如涉及一种碳化硅多晶的制造装置及方法。The present application relates to the technical field of semiconductor manufacturing, for example, to a silicon carbide polycrystalline manufacturing device and method.
背景技术Background technique
碳化硅是一种宽禁带半导体材料,以碳化硅衬底制作的器件具有耐高温、耐高压、高频、大功率、抗辐射、效率高等优势,在射频、新能源汽车等领域均具有重要的应用价值。Silicon carbide is a wide bandgap semiconductor material. Devices made of silicon carbide substrates have the advantages of high temperature resistance, high voltage resistance, high frequency, high power, radiation resistance, and high efficiency. They are important in the fields of radio frequency and new energy vehicles. application value.
碳化硅包括碳化硅单晶和碳化硅多晶。Silicon carbide includes silicon carbide single crystal and silicon carbide polycrystal.
发明内容Contents of the invention
本申请提供一种碳化硅多晶的制造装置及方法。The present application provides a silicon carbide polycrystalline manufacturing device and method.
本申请提供一种碳化硅多晶的制造装置,包括:The present application provides a silicon carbide polycrystalline manufacturing device, including:
腔室;Chamber;
感应线圈,设于所述腔室内;an induction coil is arranged in the chamber;
石墨坩埚,设于所述腔室内,且所述石墨坩埚用于容置助溶剂,且所述石墨坩埚的底部内壁能生长碳化硅多晶;A graphite crucible is arranged in the chamber, and the graphite crucible is used for accommodating a cosolvent, and the inner wall of the bottom of the graphite crucible can grow polycrystalline silicon carbide;
晶杆,所述晶杆的一端位于所述石墨坩埚内,所述晶杆的另一端位于所述腔室外;A crystal rod, one end of the crystal rod is located in the graphite crucible, and the other end of the crystal rod is located outside the chamber;
石墨托,固接于所述晶杆的一端,所述石墨托朝向所述石墨坩埚底壁的底面能生长碳化硅多晶。The graphite support is fixedly connected to one end of the crystal rod, and the bottom surface of the graphite support facing the bottom wall of the graphite crucible can grow polycrystalline silicon carbide.
本申请提供一种碳化硅多晶的制造方法,应用于上述的碳化硅多晶的制造装置,包括:The present application provides a silicon carbide polycrystalline manufacturing method, which is applied to the above-mentioned silicon carbide polycrystalline manufacturing device, including:
向石墨坩埚内放入助溶剂;Put the auxiliary solvent into the graphite crucible;
通过感应线圈加热所述助溶剂,以使所述助溶剂熔化;heating the co-solvent through an induction coil to melt the co-solvent;
通过晶杆带动石墨托靠近所述助溶剂移动,以使所述石墨托的下表面与所述助溶剂的液面平齐或间距小于预设间距;Drive the graphite support to move close to the co-solvent through the crystal rod, so that the lower surface of the graphite support is flush with the liquid level of the co-solvent or the distance is smaller than the preset distance;
控制所述晶杆带动石墨托远离所述助溶剂移动,以使在所述石墨托下表面 形成的碳化硅多晶的底面始终与所述助溶剂的液面平齐或间距小于预设间距。Controlling the crystal rod to drive the graphite holder to move away from the co-solvent, so that the lower surface of the graphite holder The bottom surface of the formed silicon carbide polycrystal is always flush with the liquid level of the co-solvent or the distance is smaller than the preset distance.
附图说明Description of drawings
图1是本申请实施例一提供的碳化硅多晶的制造装置的结构示意图;FIG. 1 is a schematic structural view of a silicon carbide polycrystalline manufacturing device provided in Embodiment 1 of the present application;
图2是本申请实施例一提供的石墨坩埚、晶杆及石墨托的装配示意图;Fig. 2 is the schematic diagram of the assembly of the graphite crucible, the crystal rod and the graphite holder provided in the first embodiment of the present application;
图3是本申请实施例一提供的石墨坩埚、晶杆及石墨托的使用状态参考图;Fig. 3 is a reference diagram of the use state of the graphite crucible, the crystal rod and the graphite support provided in the first embodiment of the present application;
图4是本申请实施例一提供的晶杆及石墨托的结构示意图;Fig. 4 is a schematic structural view of a crystal rod and a graphite holder provided in Embodiment 1 of the present application;
图5是本申请实施例一提供的晶杆的俯视图;Fig. 5 is a top view of the crystal rod provided in Embodiment 1 of the present application;
图6是本申请实施例一提供的坩埚托及石墨坩埚的结构示意图;Fig. 6 is a schematic structural view of a crucible holder and a graphite crucible provided in Embodiment 1 of the present application;
图7是本申请实施例二提供的碳化硅多晶的制造方法的流程图。FIG. 7 is a flowchart of a method for manufacturing a silicon carbide polycrystal provided in Embodiment 2 of the present application.
图中:In the picture:
1、腔室;2、感应线圈;3、石墨坩埚;4、晶杆;41、第一冷却流道;411、第一子流道;412、第二子流道;413、冷却入口;414、冷却出口;5、石墨托;6、碳膜层;7、坩埚托;71、第二冷却流道;711、第三子流道;712、第四子流道;713、入口;714、出口;8、隔热套;10、碳化硅多晶;100、助溶剂。1. Chamber; 2. Induction coil; 3. Graphite crucible; 4. Crystal rod; 41. First cooling channel; 411. First sub-channel; 412. Second sub-channel; 413. Cooling inlet; 414 , cooling outlet; 5, graphite support; 6, carbon film layer; 7, crucible support; 71, the second cooling channel; 711, the third sub-channel; 712, the fourth sub-channel; 713, the entrance; 714, Export; 8. Heat insulation sleeve; 10. Silicon carbide polycrystalline; 100. Cosolvent.
具体实施方式Detailed ways
碳化硅包括碳化硅单晶和碳化硅多晶,相关技术中,采用溶液法生长碳化硅单晶,溶液法的基本原理是:将含硅助熔剂置于石墨坩埚中,利用感应加热的方式熔化助熔剂,石墨坩埚中的碳溶解到助熔剂中;然后将碳化硅籽晶置于助熔剂的液面,由于籽晶处的过冷,碳在籽晶的固液界面上析出,并和助熔剂中的硅结合形成碳化硅单晶。但是,相关技术中没有文献记载通过溶液法如何生长碳化硅多晶。因此,亟需一种碳化硅多晶的制造装置及方法。Silicon carbide includes silicon carbide single crystal and silicon carbide polycrystal. In related technologies, a solution method is used to grow silicon carbide single crystal. The basic principle of the solution method is: put a silicon-containing flux in a graphite crucible and melt it by induction heating Flux, the carbon in the graphite crucible is dissolved in the flux; then the silicon carbide seed crystal is placed on the liquid level of the flux, and due to the supercooling of the seed crystal, carbon is precipitated on the solid-liquid interface of the seed crystal, and with the flux The silicon in the flux combines to form a single crystal of silicon carbide. However, there is no document in the related art describing how to grow silicon carbide polycrystals by a solution method. Therefore, there is an urgent need for a silicon carbide polycrystalline manufacturing device and method.
针对上述情况,本申请实施例提供一种碳化硅多晶的制造装置及方法。In view of the above situation, embodiments of the present application provide a silicon carbide polycrystalline manufacturing device and method.
下面结合附图并通过具体实施方式来说明本申请的实施例。Embodiments of the present application will be described below in conjunction with the accompanying drawings and through specific implementation methods.
在本申请的描述中,除非另有明确的规定和限定,术语“相连”、“连接”、“固定”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本申请中的具体含义。In the description of this application, unless otherwise clearly specified and limited, the terms "connected", "connected" and "fixed" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integrated ; It can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediary, and it can be the internal communication of two components or the interaction relationship between two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in this application in specific situations.
在本申请中,除非另有明确的规定和限定,第一特征在第二特征之“上” 或之“下”可以包括第一和第二特征直接接触,也可以包括第一和第二特征不是直接接触而是通过它们之间的另外的特征接触。而且,第一特征在第二特征“之上”、“上方”和“上面”包括第一特征在第二特征正上方和斜上方,或仅仅表示第一特征水平高度高于第二特征。第一特征在第二特征“之下”、“下方”和“下面”包括第一特征在第二特征正下方和斜下方,或仅仅表示第一特征水平高度小于第二特征。In this application, unless otherwise expressly specified and limited, the first feature is "on" the second feature Alternatively, "under" may include that the first and second features are in direct contact, and may also include that the first and second features are not in direct contact but are in contact through another feature therebetween. Moreover, "above", "above" and "above" the first feature on the second feature include that the first feature is directly above and obliquely above the second feature, or simply means that the first feature is horizontally higher than the second feature. "Below", "beneath" and "under" the first feature to the second feature include that the first feature is directly below and obliquely below the second feature, or simply means that the first feature has a lower level than the second feature.
在本实施例的描述中,术语“上”、“下”、“右”、等方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述和简化操作,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。此外,术语“第一”、“第二”仅仅用于在描述上加以区分,并没有特殊的含义。In the description of this embodiment, the terms "up", "down", "right", and other orientations or positional relationships are based on the orientations or positional relationships shown in the drawings, and are only for the convenience of description and simplification of operations, rather than indicating Or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation, and therefore should not be construed as limiting the application. In addition, the terms "first" and "second" are only used to distinguish in description, and have no special meaning.
实施例一Embodiment one
本实施例提供了一种碳化硅多晶的制造装置,能够用于生长制造碳化硅多晶,具有较高的效率和较低的成本。This embodiment provides a silicon carbide polycrystalline manufacturing device, which can be used to grow and manufacture silicon carbide polycrystalline, and has higher efficiency and lower cost.
如图1所示,碳化硅多晶的制造装置包括腔室1、感应线圈2、石墨坩埚3、晶杆4及石墨托5。As shown in FIG. 1 , a silicon carbide polycrystalline manufacturing device includes a chamber 1 , an induction coil 2 , a graphite crucible 3 , a crystal rod 4 and a graphite holder 5 .
其中,腔体1用于为碳化硅多晶的生长提供相对密封的空间,且腔室1具有至少一个抽气口,通过抽气口能对腔室1抽真空。在一些实施例中,抽气口与真空装置连接,使得真空装置能够通过抽气口对腔室1进行抽气,以将腔室1内的气压降低至所需的数值。需要说明的是,腔室1还连接至少一个真空计,真空计用于测量腔室1内的压力。本实施例中,腔体1还具有至少一个充气口,通过充气口可以向腔室1内充入氮气、氩气、氦气或其他惰性气体,以使得碳化硅多晶能够在惰性气体环境下生长。Wherein, the cavity 1 is used to provide a relatively sealed space for the growth of polycrystalline silicon carbide, and the cavity 1 has at least one gas extraction port, through which the cavity 1 can be evacuated. In some embodiments, the pumping port is connected to a vacuum device, so that the vacuum device can pump the chamber 1 through the pumping port, so as to reduce the air pressure in the chamber 1 to a required value. It should be noted that the chamber 1 is also connected with at least one vacuum gauge, and the vacuum gauge is used to measure the pressure in the chamber 1 . In this embodiment, the chamber 1 also has at least one gas filling port, through which nitrogen, argon, helium or other inert gases can be filled into the chamber 1, so that the silicon carbide polycrystalline grow.
感应线圈2和石墨坩埚3分别设于腔室1内,且石墨坩埚3用于容置助溶剂。如图2所示,感应线圈2用于对石墨坩埚3内的助溶剂100进行感应加热,使得石墨坩埚3中的助溶剂100熔融。在一些实施例中,感应线圈2有多个匝,围绕石墨坩埚3间隔设置,以实现均匀加热。感应线圈2的电流频率为1~100kHz,且感应线圈2是中空结构的,能够通水冷却。感应线圈2感应加热的原理可以参见相关技术,本实施例在此不做介绍。The induction coil 2 and the graphite crucible 3 are respectively arranged in the chamber 1, and the graphite crucible 3 is used for accommodating a cosolvent. As shown in FIG. 2 , the induction coil 2 is used to inductively heat the co-solvent 100 in the graphite crucible 3 to melt the co-solvent 100 in the graphite crucible 3 . In some embodiments, the induction coil 2 has multiple turns, which are arranged at intervals around the graphite crucible 3 to achieve uniform heating. The current frequency of the induction coil 2 is 1-100kHz, and the induction coil 2 is hollow and can be cooled by water. For the principle of induction heating by the induction coil 2 , reference may be made to related technologies, which will not be introduced here in this embodiment.
晶杆4的一端位于石墨坩埚3内,晶杆4的另一端位于腔室1外,石墨托5固接于晶杆4的一端并位于石墨坩埚3内,晶杆4能够带动石墨托5相对于石墨坩埚3移动,如带动石墨托5旋转或沿图1中的上下方向移动。在一些实施 例中,晶杆4的另一端连接有驱动件,驱动件能够向晶杆4提供驱动力。One end of the crystal rod 4 is located in the graphite crucible 3, the other end of the crystal rod 4 is located outside the chamber 1, and the graphite holder 5 is fixedly connected to one end of the crystal rod 4 and is located in the graphite crucible 3, and the crystal rod 4 can drive the graphite holder 5 to be opposite to each other. The graphite crucible 3 moves, such as driving the graphite holder 5 to rotate or move along the up and down direction in FIG. 1 . in some implementations In an example, the other end of the crystal rod 4 is connected with a driving member, and the driving member can provide driving force to the crystal rod 4 .
石墨托5朝向石墨坩埚3底壁的底面及石墨坩埚3的底部内壁均能够生长碳化硅多晶,使得在一次工艺中,能够得到多块碳化硅多晶。Both the bottom surface of the graphite holder 5 facing the bottom wall of the graphite crucible 3 and the bottom inner wall of the graphite crucible 3 can grow silicon carbide polycrystals, so that multiple pieces of silicon carbide polycrystals can be obtained in one process.
本实施例提供的碳化硅多晶的制造装置,能够采用溶液法制造碳化硅多晶,通过设置石墨托5和石墨坩埚3,能够实现直接在石墨材料上结晶,进而得到碳化硅多晶,无需设置籽晶,且石墨托5和石墨坩埚3上能够同时结晶,使得一个装置能够同时得到两块碳化硅多晶,提高了碳化硅多晶的制造效率,降低了制造碳化硅多晶的成本。The silicon carbide polycrystalline manufacturing device provided in this embodiment can adopt the solution method to manufacture silicon carbide polycrystalline. By setting the graphite holder 5 and the graphite crucible 3, it can realize direct crystallization on the graphite material, and then obtain the silicon carbide polycrystalline. The seed crystal is set, and the graphite holder 5 and the graphite crucible 3 can be crystallized at the same time, so that one device can obtain two silicon carbide polycrystals at the same time, which improves the manufacturing efficiency of silicon carbide polycrystals and reduces the cost of manufacturing silicon carbide polycrystals.
在一实施例中,如图3所示,石墨坩埚3的底部内壁固设有碳膜层6,碳膜层6的设置能够减小结晶过程的应力,避免生长的碳化硅多晶出现开裂的情况,同时,还能够便于碳化硅多晶与石墨坩埚3的分离,避免因碳化硅多晶与石墨坩埚3之间粘接过于牢固而发生破坏性分离,保证了碳化硅多晶的质量。需要说明的是,碳膜层6能够完全覆盖石墨坩埚3的底部内壁,以保证碳化硅多晶的生长均匀性及生长面积。In one embodiment, as shown in Figure 3, the inner wall of the bottom of the graphite crucible 3 is fixed with a carbon film layer 6, the setting of the carbon film layer 6 can reduce the stress of the crystallization process, and avoid the occurrence of cracks in the grown silicon carbide polycrystalline At the same time, it can also facilitate the separation of the silicon carbide polycrystal and the graphite crucible 3, avoid destructive separation due to too strong bonding between the silicon carbide polycrystal and the graphite crucible 3, and ensure the quality of the silicon carbide polycrystal. It should be noted that the carbon film layer 6 can completely cover the bottom inner wall of the graphite crucible 3 to ensure the growth uniformity and growth area of the silicon carbide polycrystal.
类似地,石墨托5的底面具有碳膜层6,此时,碳膜层6能够便于碳化硅多晶与石墨托5之间的分离,保证了在石墨托5上生长的碳化硅多晶的质量。需要说明的是,碳膜层6能够完全覆盖石墨托5的底面,以保证碳化硅多晶的生长均匀性及生长面积。Similarly, the bottom surface of the graphite holder 5 has a carbon film layer 6. At this time, the carbon film layer 6 can facilitate the separation between the silicon carbide polycrystal and the graphite holder 5, ensuring the stability of the silicon carbide polycrystal grown on the graphite holder 5. quality. It should be noted that the carbon film layer 6 can completely cover the bottom surface of the graphite support 5 to ensure the growth uniformity and growth area of the silicon carbide polycrystal.
本实施例中,碳膜层6可以通过化学气相沉积法制备获得,还可以通过物理气相沉积、磁控溅射、电子束蒸发、涂覆石墨胶或糖胶后高温固化等方法进行沉积获得,本实施例对此不作限定。In this embodiment, the carbon film layer 6 can be prepared by chemical vapor deposition, and can also be deposited by physical vapor deposition, magnetron sputtering, electron beam evaporation, high-temperature curing after coating graphite glue or sugar glue, etc. This embodiment does not limit it.
如图3所示,经过一段时间的生长,能够在石墨托5的底面的碳膜层6下方得到块状的碳化硅多晶10,并能够在石墨坩埚3底部的碳膜层6上得到块状的碳化硅多晶10。其中,石墨坩埚3的底面通过碳膜层6与碳化硅多晶10连接,碳化硅多晶10与石墨坩埚3的侧壁可能会发生粘接,即碳化硅多晶10出现贴锅生长,为了便于碳化硅多晶10与石墨坩埚3的侧壁顺利地分离,可以在石墨坩埚3的侧壁镀设一定高度的碳膜层6,使得在不妨碍石墨坩埚3中的碳溶解在助溶剂100中的前提下,碳化硅多晶10与石墨坩埚3能够更好地分离。在碳化硅多晶的制造装置冷却后,可以将碳化硅多晶10与石墨托5上的碳膜层6分离,以及将碳化硅多晶10与石墨坩埚3底部的碳膜层6分离。As shown in Figure 3, after a period of growth, blocky silicon carbide polycrystal 10 can be obtained under the carbon film layer 6 on the bottom surface of the graphite holder 5, and block can be obtained on the carbon film layer 6 at the bottom of the graphite crucible 3 SiC polycrystalline 10. Wherein, the bottom surface of the graphite crucible 3 is connected with the silicon carbide polycrystal 10 through the carbon film layer 6, and the sidewall of the silicon carbide polycrystal 10 and the graphite crucible 3 may be bonded, that is, the silicon carbide polycrystal 10 appears sticking to the pot and grows. To facilitate the smooth separation of the silicon carbide polycrystalline 10 and the sidewall of the graphite crucible 3, a carbon film layer 6 of a certain height can be plated on the sidewall of the graphite crucible 3, so that the carbon in the graphite crucible 3 is dissolved in the cosolvent 100 without hindering it. Under the premise of , the polycrystalline silicon carbide 10 and the graphite crucible 3 can be separated better. After the silicon carbide polycrystalline manufacturing device is cooled, the silicon carbide polycrystalline 10 can be separated from the carbon film layer 6 on the graphite support 5 , and the silicon carbide polycrystalline 10 can be separated from the carbon film layer 6 at the bottom of the graphite crucible 3 .
在一实施例中,本实施例中的碳膜层6的厚度为1~1000微米,例如,碳膜层6的厚度为10~100微米。 In an embodiment, the thickness of the carbon film layer 6 in this embodiment is 1-1000 microns, for example, the thickness of the carbon film layer 6 is 10-100 microns.
本实施例中,如图4所示,晶杆4具有第一冷却流道41,第一冷却流道41中的冷却流体用于冷却石墨托5。由于在碳化硅多晶形成的过程中,需要石墨托5处的过冷,使得助溶剂100中的碳在石墨托5及助溶剂100的固液界面上析出,并与助溶剂中的硅结合形成碳化硅多晶,因此,为了保证石墨托5处具有达到要求的过冷,可以在晶杆4上设置第一冷却流道41,通过第一冷却流道41带走石墨托5上的热量,使得石墨托5处于过冷状态。在一些实施例中,第一冷却流道41经过晶杆4连接石墨托5的一端,以能够较好地冷却石墨托5。In this embodiment, as shown in FIG. 4 , the crystal rod 4 has a first cooling channel 41 , and the cooling fluid in the first cooling channel 41 is used to cool the graphite holder 5 . Due to the need for supercooling at the graphite support 5 during the formation of silicon carbide polycrystals, the carbon in the co-solvent 100 is precipitated on the solid-liquid interface between the graphite support 5 and the co-solvent 100, and combines with the silicon in the co-solvent Silicon carbide polycrystalline is formed, therefore, in order to ensure that the graphite support 5 has the required supercooling, a first cooling flow channel 41 can be set on the crystal rod 4, and the heat on the graphite support 5 can be taken away by the first cooling flow channel 41 , so that the graphite support 5 is in a supercooled state. In some embodiments, the first cooling channel 41 is connected to one end of the graphite support 5 through the crystal rod 4 to better cool the graphite support 5 .
在一实施例中,在第一冷却流道41中流动的冷却流体可以为氦气,本实施例中,可以控制第一冷却流道41中氦气的流量,进而控制石墨托5附近的温度梯度,从而实现控制石墨托5上碳化硅多晶的生长速度和质量,使得得到的碳化硅多晶满足要求。In one embodiment, the cooling fluid flowing in the first cooling channel 41 can be helium. In this embodiment, the flow rate of helium in the first cooling channel 41 can be controlled, thereby controlling the temperature near the graphite support 5 Gradient, so as to control the growth rate and quality of silicon carbide polycrystals on the graphite support 5, so that the obtained silicon carbide polycrystals meet the requirements.
在一实施例中,如图4所示,晶杆4包括第一管体42及套设于第一管体42外的第二管体43,在一些实施例中,第一管体42悬空于第二管体43中。第二管体43的一端固接于石墨托5,第二管体43的另一端伸出腔室1。第一冷却流道41包括由第一管体42形成的第一子流道411及由第一管体42与第二管体43之间的空隙形成的第二子流道412,第一子流道411与第二子流道412连通,使得冷却流体可以由第一子流道411流入第二子流道412或由第二子流道412流入第一子流道411,进而形成环路。在一些实施例中,第一管体42靠近第二管体43一端的第一端为开口端,且第一管体42的第一端与第二管体43的一端间隔设置,使得第一管体42中的冷却流体能够由第一管体42的第一端流出并进入第一管体42与第二管体43之间,第二管体43的一端为封口端或开口端,当第二管体43的一端为开口端时,第二管体43与石墨托5密封连接。在另外一些实施例中,第一管体42靠近第二管体43一端的第一端为封口端。并且,第一管体42的第一端的管壁设有通孔,第一管体42中的冷却流体能够通过通孔流入第一管体42与第二管体43之间。In one embodiment, as shown in FIG. 4, the crystal rod 4 includes a first tube body 42 and a second tube body 43 sleeved outside the first tube body 42. In some embodiments, the first tube body 42 is suspended in the air. in the second pipe body 43 . One end of the second tube body 43 is fixedly connected to the graphite holder 5 , and the other end of the second tube body 43 extends out of the chamber 1 . The first cooling channel 41 includes a first sub-channel 411 formed by the first tube body 42 and a second sub-channel 412 formed by the gap between the first tube body 42 and the second tube body 43. The flow channel 411 communicates with the second sub-channel 412, so that the cooling fluid can flow from the first sub-channel 411 into the second sub-channel 412 or from the second sub-channel 412 into the first sub-channel 411, thereby forming a loop . In some embodiments, the first end of the first tube body 42 close to the end of the second tube body 43 is an open end, and the first end of the first tube body 42 is spaced apart from one end of the second tube body 43, so that the first The cooling fluid in the pipe body 42 can flow out from the first end of the first pipe body 42 and enter between the first pipe body 42 and the second pipe body 43. One end of the second pipe body 43 is a sealed end or an open end. When one end of the second pipe body 43 is an open end, the second pipe body 43 is sealed and connected with the graphite holder 5 . In some other embodiments, the first end of the first tube body 42 close to the end of the second tube body 43 is a sealed end. Moreover, the first end of the first pipe body 42 is provided with a through hole, and the cooling fluid in the first pipe body 42 can flow into the space between the first pipe body 42 and the second pipe body 43 through the through hole.
需要说明的是,第一管体42与第二管体43能够发生相对运动,例如,在需要带动石墨托5旋转时,可以直接驱动第二管体43转动,而第一管体42保持静止。It should be noted that the first tube body 42 and the second tube body 43 can move relative to each other. For example, when the graphite holder 5 needs to be driven to rotate, the second tube body 43 can be directly driven to rotate, while the first tube body 42 remains stationary. .
在一实施例中,第一管体42远离第二管体43一端的第二端的端面可以与第二管体43的端面平齐,也即是,晶杆4未连接石墨托5一端的端面为平面,请继续参见图4,第一冷却流道41具有位于晶杆4端面的冷却入口413及冷却出口414,冷却流道能够通过冷却入口413流入第一冷却流道41,例如流入第 一子流道411,并流动至石墨托5附近,吸收石墨托5的热量后,经第二子流道412并由冷却出口414流出。如图5所示,本实施例中的冷却入口413为中心孔,冷却出口414为围绕冷却入口413设置的环形孔。可以理解的是,晶杆4未连接石墨托5一端的端面还可以不是平面,也即是,第一管体42的长度大于第二管体43的长度。在一些实施例中,第一冷却流道41可以连通于驱动泵,驱动泵为第一冷却流道41中的氦气提供驱动力,当晶杆4包括第一管体42时,第一管体42连接于驱动泵。In one embodiment, the end surface of the second end of the first tube body 42 away from the end of the second tube body 43 can be flush with the end surface of the second tube body 43, that is, the end surface of the end surface of the crystal rod 4 not connected to the graphite holder 5 It is a plane, please continue to refer to FIG. 4, the first cooling channel 41 has a cooling inlet 413 and a cooling outlet 414 located at the end surface of the crystal rod 4, and the cooling channel can flow into the first cooling channel 41 through the cooling inlet 413, for example, into the first cooling channel 41. A sub-channel 411 , and flows to the vicinity of the graphite holder 5 , absorbs the heat of the graphite holder 5 , passes through the second sub-channel 412 and flows out from the cooling outlet 414 . As shown in FIG. 5 , the cooling inlet 413 in this embodiment is a central hole, and the cooling outlet 414 is an annular hole arranged around the cooling inlet 413 . It can be understood that the end surface of the crystal rod 4 not connected to the graphite holder 5 may not be a plane, that is, the length of the first tube body 42 is greater than the length of the second tube body 43 . In some embodiments, the first cooling channel 41 may be connected to a driving pump, and the driving pump provides driving force for the helium in the first cooling channel 41. When the crystal rod 4 includes a first tube body 42, the first tube Body 42 is connected to the drive pump.
请继续参见图1,碳化硅多晶的制造装置还包括坩埚托7。其中,坩埚托7的一端固接于石墨坩埚3的底壁,坩埚托7的另一端位于腔室1外。在一些实施例中,坩埚托7能带动石墨坩埚3旋转。在一实施例中,坩埚托7能够在驱动机构的驱动下旋转,进而带动石墨坩埚旋转。本实施例中,坩埚托7还可以带动石墨坩埚3在图1所示的上下方向移动,以调整石墨坩埚3在感应线圈2中的位置。在一些实施例中,坩埚托7的旋转方向与晶杆4的旋转方向相反;在另外一些实施例中,也可以周期性地改变坩埚托7或晶杆4的旋转速度或周期性地正转和反转。Please continue to refer to FIG. 1 , the silicon carbide polycrystalline manufacturing device also includes a crucible holder 7 . Wherein, one end of the crucible holder 7 is fixedly connected to the bottom wall of the graphite crucible 3 , and the other end of the crucible holder 7 is located outside the chamber 1 . In some embodiments, the crucible holder 7 can drive the graphite crucible 3 to rotate. In one embodiment, the crucible holder 7 can rotate under the drive of the driving mechanism, thereby driving the graphite crucible to rotate. In this embodiment, the crucible holder 7 can also drive the graphite crucible 3 to move in the up and down direction shown in FIG. 1 to adjust the position of the graphite crucible 3 in the induction coil 2 . In some embodiments, the rotation direction of the crucible holder 7 is opposite to the rotation direction of the crystal rod 4; in other embodiments, the rotation speed of the crucible holder 7 or the crystal rod 4 may also be periodically changed or rotated forward periodically and reverse.
在一实施例中,如图6所示,坩埚托7具有第二冷却流道71,第二冷却流道71中的冷却流体用于冷却石墨坩埚3的底壁。由于在碳化硅多晶形成的过程中,需要石墨坩埚3处的过冷,使得助溶剂100中的碳在石墨坩埚3及助溶剂100的固液界面上析出,并与助溶剂中的硅结合形成碳化硅多晶,因此,为了保证石墨坩埚3处具有达到要求的过冷,可以在坩埚托7上设置第二冷却流道71,通过第二冷却流道71带走石墨坩埚3上的热量,使得石墨坩埚3处于过冷状态。在一些实施例中,第二冷却流道71经过坩埚托7连接石墨坩埚3的一端,以能够较好地冷却石墨坩埚3。In one embodiment, as shown in FIG. 6 , the crucible holder 7 has a second cooling channel 71 , and the cooling fluid in the second cooling channel 71 is used to cool the bottom wall of the graphite crucible 3 . Due to the need for supercooling at the graphite crucible 3 during the formation of silicon carbide polycrystals, the carbon in the co-solvent 100 is precipitated on the solid-liquid interface between the graphite crucible 3 and the co-solvent 100, and combines with the silicon in the co-solvent Form silicon carbide polycrystal, therefore, in order to ensure that the graphite crucible 3 place has the required supercooling, a second cooling flow channel 71 can be set on the crucible holder 7, and the heat on the graphite crucible 3 can be taken away by the second cooling flow channel 71 , so that the graphite crucible 3 is in a supercooled state. In some embodiments, the second cooling channel 71 is connected to one end of the graphite crucible 3 through the crucible holder 7 so as to better cool the graphite crucible 3 .
在一实施例中,在第二冷却流道71中流动的冷却流体可以为氦气,本实施例中,可以控制第二冷却流道71中氦气的流量,进而控制石墨坩埚3附近的温度梯度,从而实现控制石墨坩埚3上碳化硅多晶的生长速度和质量,使得得到的碳化硅多晶满足要求。In one embodiment, the cooling fluid flowing in the second cooling channel 71 can be helium, in this embodiment, the flow rate of helium in the second cooling channel 71 can be controlled, and then the temperature near the graphite crucible 3 can be controlled Gradient, so as to realize the control of the growth rate and quality of the silicon carbide polycrystal on the graphite crucible 3, so that the obtained silicon carbide polycrystal meets the requirements.
在一实施例中,如图6所示,坩埚托7包括第三管体72及套设于第三管体72外的第四管体73,在一些实施例中,第三管体72悬空于第四管体73中。第四管体73的一端固接于石墨坩埚3,第四管体73的另一端伸出腔室1。第二冷却流道71包括由第三管体72形成的第三子流道711及由第三管体72与第四管体73之间的空隙形成的第四子流道712,第三子流道711与第四子流道712连 通,使得冷却流体可以由第三子流道711流入第四子流道712或由第四子流道712流入第三子流道711,进而形成环路。在一些实施例中,第三管体72靠近第四管体73一端的第三端为开口端,且第三管体72的第三端与第四管体73的一端间隔设置,使得第三管体72中的冷却流体能够由第三管体72的第三端流出并进入第三管体72与第四管体73之间,第四管体73的一端为封口端或开口端,当第四管体73的一端为开口端时,第四管体73与石墨坩埚3密封连接。在另外一些实施例中,第三管体72靠近第四管体73一端的第三端为封口端。并且,第三管体72的第三端的管壁设有通孔,第三管体72中的冷却流体能够通过第三管体72上的通孔流入第三管体72与第四管体73之间。In one embodiment, as shown in FIG. 6, the crucible holder 7 includes a third tube body 72 and a fourth tube body 73 sleeved outside the third tube body 72. In some embodiments, the third tube body 72 is suspended in the air. in the fourth tube body 73 . One end of the fourth tube body 73 is fixedly connected to the graphite crucible 3 , and the other end of the fourth tube body 73 extends out of the chamber 1 . The second cooling channel 71 includes a third sub-channel 711 formed by the third tube body 72 and a fourth sub-channel 712 formed by the gap between the third tube body 72 and the fourth tube body 73. The runner 711 is connected with the fourth sub-runner 712 so that the cooling fluid can flow from the third sub-channel 711 into the fourth sub-channel 712 or from the fourth sub-channel 712 into the third sub-channel 711, thereby forming a loop. In some embodiments, the third end of the third pipe body 72 close to the end of the fourth pipe body 73 is an open end, and the third end of the third pipe body 72 is spaced from the end of the fourth pipe body 73, so that the third The cooling fluid in the pipe body 72 can flow out from the third end of the third pipe body 72 and enter between the third pipe body 72 and the fourth pipe body 73. One end of the fourth pipe body 73 is a sealed end or an open end. When one end of the fourth pipe body 73 is an open end, the fourth pipe body 73 is in sealing connection with the graphite crucible 3 . In some other embodiments, the third end of the third tube body 72 close to the end of the fourth tube body 73 is a sealed end. Moreover, the pipe wall at the third end of the third pipe body 72 is provided with a through hole, and the cooling fluid in the third pipe body 72 can flow into the third pipe body 72 and the fourth pipe body 73 through the through hole on the third pipe body 72 between.
需要说明的是,第三管体72与第四管体73能够发生相对运动,例如,在需要带动石墨坩埚3旋转时,可以直接驱动第四管体73转动,而第三管体72保持静止。It should be noted that the third pipe body 72 and the fourth pipe body 73 can move relative to each other. For example, when the graphite crucible 3 needs to be driven to rotate, the fourth pipe body 73 can be directly driven to rotate, while the third pipe body 72 remains stationary .
在一实施例中,第三管体72远离第四管体73一端的第四端的端面可以与第四管体73的端面平齐,也即是,坩埚托7未连接石墨坩埚3一端的端面为平面,请继续参见图6,第二冷却流道71具有位于坩埚托7端面的一个入口713及一个出口714,冷却流道能够通过入口713流入第二冷却流道71,例如流入第三子流道711,并流动至石墨坩埚3附近,吸收石墨坩埚3的热量后,经第四子流道712并由出口714流出。本实施例中的入口713为中心孔,出口714为围绕入口713设置的环形孔。可以理解的是,坩埚托7未连接石墨坩埚3一端的端面还可以不是平面,也即是,第三管体72的长度大于第四管体73的长度。在一些实施例中,第二冷却流道71可以连通于驱动泵,驱动泵为第二冷却流道71中的氦气提供驱动力,当坩埚托7包括第三管体72时,第三管体72连接于驱动泵。In one embodiment, the end face of the fourth end of the third pipe body 72 away from the end of the fourth pipe body 73 can be flush with the end face of the fourth pipe body 73, that is, the end face of the end face of the crucible holder 7 that is not connected to the graphite crucible 3 It is a plane, please continue to refer to FIG. 6, the second cooling channel 71 has an inlet 713 and an outlet 714 on the end surface of the crucible holder 7, the cooling channel can flow into the second cooling channel 71 through the inlet 713, for example, into the third sub- flow channel 711 , and flow to the vicinity of the graphite crucible 3 , absorb the heat of the graphite crucible 3 , pass through the fourth sub-channel 712 and flow out from the outlet 714 . In this embodiment, the inlet 713 is a central hole, and the outlet 714 is an annular hole arranged around the inlet 713 . It can be understood that the end surface of the crucible holder 7 not connected to the end of the graphite crucible 3 may not be a plane, that is, the length of the third tube body 72 is greater than the length of the fourth tube body 73 . In some embodiments, the second cooling channel 71 may be connected to a driving pump, and the driving pump provides driving force for the helium in the second cooling channel 71. When the crucible holder 7 includes a third tube body 72, the third tube Body 72 is connected to the drive pump.
如图1所示,碳化硅多晶的制造装置还包括隔热套8,石墨坩埚3设置于隔热套8内,感应线圈2位于隔热套8外,坩埚托7及晶杆4分别穿设于隔热套8,隔热套8采用隔热材质制成,并用于石墨坩埚3的保温隔热。As shown in Figure 1, the silicon carbide polycrystalline manufacturing device also includes a heat insulating cover 8, the graphite crucible 3 is arranged in the heat insulating cover 8, the induction coil 2 is located outside the heat insulating cover 8, and the crucible holder 7 and the crystal rod 4 respectively pass through the heat insulating cover 8. Set in the heat insulation sleeve 8, the heat insulation sleeve 8 is made of heat insulation material, and is used for heat insulation of the graphite crucible 3.
本实施例提供的碳化硅多晶的制造装置能够在一次制造工艺中形成两块碳化硅多晶,提高了碳化硅多晶的制造效率,且具有较低的成本。The silicon carbide polycrystal manufacturing device provided in this embodiment can form two silicon carbide polycrystals in one manufacturing process, which improves the manufacturing efficiency of the silicon carbide polycrystal and has a lower cost.
实施例二Embodiment two
本实施例提供了一种碳化硅多晶的制造方法,应用于实施例一中的碳化硅多晶的制造装置,如图7所示,碳化硅多晶的制造方法包括如下步骤:This embodiment provides a silicon carbide polycrystalline manufacturing method, which is applied to the silicon carbide polycrystalline manufacturing device in Embodiment 1. As shown in FIG. 7, the silicon carbide polycrystalline manufacturing method includes the following steps:
S1、向石墨坩埚3内放入助溶剂100。 S1. Put the auxiliary solvent 100 into the graphite crucible 3 .
需要说明的是,本实施例中的助溶剂100为含硅元素的助溶剂,以使得助溶剂100中的硅能与碳形成碳化硅多晶。可以理解的是,除了硅之外,助溶剂100还可以包括钛Ti、铬Cr、钪Sc、镍Ni、铝Al、钴Co、锰Mn、镁Mg、锗Ge、砷As、硼P、氮N、氧O、硼B、镝Dy、钇Y、铌Nb、钕Nd、铁Fe中的一种或多种元素。It should be noted that the co-solvent 100 in this embodiment is a co-solvent containing silicon, so that silicon in the co-solvent 100 can form silicon carbide polycrystals with carbon. It can be understood that, in addition to silicon, the co-solvent 100 can also include titanium Ti, chromium Cr, scandium Sc, nickel Ni, aluminum Al, cobalt Co, manganese Mn, magnesium Mg, germanium Ge, arsenic As, boron P, nitrogen One or more elements of N, oxygen O, boron B, dysprosium Dy, yttrium Y, niobium Nb, neodymium Nd, and iron Fe.
S2、通过感应线圈2加热助溶剂,以使助溶剂100熔化。S2 , heating the co-solvent through the induction coil 2 to melt the co-solvent 100 .
在步骤S2中,感应线圈2通电,使感应线圈2加热并熔化助溶剂100,使得助溶剂100呈液态。In step S2, the induction coil 2 is energized to heat the induction coil 2 and melt the co-solvent 100, so that the co-solvent 100 is in a liquid state.
S3、通过晶杆4带动石墨托5靠近助溶剂100移动,以使石墨托5的下表面与助溶剂100的液面平齐或间距小于预设间距。S3. Drive the graphite support 5 to move close to the co-solvent 100 through the crystal rod 4, so that the lower surface of the graphite support 5 is flush with the liquid level of the co-solvent 100 or the distance is smaller than the preset distance.
石墨托5的下表面与助溶剂100的液面平齐是指石墨托5的下表面刚好与助溶剂100的液面接触。预设间距最大为5毫米,以保证顺利生长碳化硅多晶。需要说明的是,当石墨托5的下表面设有碳膜层6时,控制碳膜层6的下表面与助溶剂100的液面平齐或间距小于预设间距。The fact that the lower surface of the graphite support 5 is flush with the liquid surface of the co-solvent 100 means that the lower surface of the graphite support 5 is just in contact with the liquid surface of the co-solvent 100 . The preset spacing is up to 5mm to ensure the smooth growth of SiC polycrystalline. It should be noted that, when the lower surface of the graphite support 5 is provided with the carbon film layer 6, the lower surface of the carbon film layer 6 is controlled to be flush with the liquid level of the co-solvent 100 or the distance is smaller than the preset distance.
S4、控制晶杆4带动石墨托5远离助溶剂100移动,以使在石墨托5下表面形成的碳化硅多晶的底面始终与助溶剂100的液面平齐或间距小于预设间距。S4. Control the crystal rod 4 to drive the graphite support 5 to move away from the co-solvent 100, so that the bottom surface of the polycrystalline silicon carbide formed on the lower surface of the graphite support 5 is always flush with the liquid level of the co-solvent 100 or the distance is smaller than the preset distance.
随着碳化硅多晶的生长,需要控制碳化硅多晶的底面始终与助溶剂的液面平齐或间距小于预设间距,进而保证碳化硅多晶生长一定的厚度。需要说明的是,石墨托5的下表面及石墨坩埚3底部的内壁均能够生长碳化硅多晶。With the growth of polycrystalline silicon carbide, it is necessary to control the bottom surface of polycrystalline silicon carbide to be always flush with the liquid level of the co-solvent or the distance is smaller than the preset distance, so as to ensure a certain thickness of polycrystalline silicon carbide growth. It should be noted that both the lower surface of the graphite holder 5 and the inner wall at the bottom of the graphite crucible 3 can grow polycrystalline silicon carbide.
在一实施例中,当碳化硅多晶的制造装置包括坩埚托7,且坩埚体7具有第二冷却流道71,晶杆4具有第一冷却流道41时,在步骤S4中,可以同时控制第一冷却流道41和第二冷却流道71中的冷却流体的流量,从而控制石墨托5和石墨坩埚3附近的温度梯度,进而控制碳化硅多晶的生长速度和质量。In one embodiment, when the silicon carbide polycrystalline manufacturing device includes a crucible holder 7, and the crucible body 7 has a second cooling flow channel 71, and the crystal rod 4 has a first cooling flow channel 41, in step S4, simultaneously The flow rate of the cooling fluid in the first cooling channel 41 and the second cooling channel 71 is controlled, thereby controlling the temperature gradient near the graphite support 5 and the graphite crucible 3 , and then controlling the growth rate and quality of the silicon carbide polycrystal.
本实施例提供的碳化硅多晶的制造方法,能够采用溶液法制造碳化硅多晶,通过设置石墨托5和石墨坩埚3,能够实现直接在石墨材料上结晶,进而得到碳化硅多晶,无需设置籽晶,且石墨托5和石墨坩埚3上能够同时结晶,使得一个装置能够同时得到两块碳化硅多晶,提高了碳化硅多晶的制造效率,降低了制造碳化硅多晶的成本。The silicon carbide polycrystalline manufacturing method provided in this embodiment can adopt the solution method to manufacture silicon carbide polycrystalline, and by setting the graphite support 5 and the graphite crucible 3, it can realize direct crystallization on the graphite material, and then obtain the silicon carbide polycrystalline, without The seed crystal is set, and the graphite holder 5 and the graphite crucible 3 can be crystallized at the same time, so that one device can obtain two silicon carbide polycrystals at the same time, which improves the manufacturing efficiency of silicon carbide polycrystals and reduces the cost of manufacturing silicon carbide polycrystals.
本实施例中,通过控制碳化硅多晶的生长环境及助溶剂100的参数,能够得到p型碳化硅多晶和n型碳化硅多晶。In this embodiment, the p-type silicon carbide polycrystal and the n-type silicon carbide polycrystal can be obtained by controlling the growth environment of the silicon carbide polycrystal and the parameters of the cosolvent 100 .
例如,在制造p型碳化硅多晶时,石墨坩埚3的底部内壁及石墨托5的底面分别具有碳膜层6,上述碳化硅多晶的制造方法还包括向腔室1内充入氦气, 使得腔室1内的气体压强为0.5-1个大气压,并且,调节助溶剂100包括Si元素、Cr元素和Al元素,且通过感应线圈2控制助溶剂100的温度为1800℃。在步骤S4中,控制晶杆4带动石墨托5远离助溶剂移动的同时带动石墨托5旋转,例如,晶杆4的提拉速度为1-2毫米/小时,并且,控制石墨坩埚3以相反于石墨托5旋转方向的方向旋转,以同时在石墨托5下方的碳膜层6上及石墨坩埚3底壁的碳膜层6上结晶,得到两块p型碳化硅多晶。本实施例中得到的p型碳化硅多晶电阻率低于30mΩ·cm(毫欧姆·厘米)。For example, when manufacturing p-type silicon carbide polycrystals, the bottom inner wall of the graphite crucible 3 and the bottom surface of the graphite holder 5 have a carbon film layer 6 respectively, and the above-mentioned silicon carbide polycrystal manufacturing method also includes filling helium into the chamber , The gas pressure in the chamber 1 is 0.5-1 atmosphere, and the co-solvent 100 is adjusted to include Si, Cr and Al elements, and the temperature of the co-solvent 100 is controlled to 1800° C. through the induction coil 2 . In step S4, the crystal rod 4 is controlled to drive the graphite holder 5 to move away from the cosolvent while driving the graphite holder 5 to rotate, for example, the pulling speed of the crystal rod 4 is 1-2 mm/hour, and the graphite crucible 3 is controlled to reversely Rotate in the direction of the rotation direction of the graphite holder 5 to simultaneously crystallize on the carbon film layer 6 below the graphite holder 5 and on the carbon film layer 6 on the bottom wall of the graphite crucible 3 to obtain two p-type silicon carbide polycrystals. The resistivity of the p-type silicon carbide polycrystalline obtained in this embodiment is lower than 30 mΩ·cm (milliohm·cm).
例如,在制造n型碳化硅多晶时,石墨坩埚3的底部内壁及石墨托5的底面分别具有碳膜层6,碳化硅多晶的制造方法还包括向腔室1内充入氦气及氮气。需要说明的是,氮气以固定的流量充入腔室1内,碳化硅多晶的主要生长气氛为氦气。并控制腔室1内的气体压强为0.5-1个大气压,助溶剂包括Si元素和Cr元素,且助溶剂的温度为2000℃。在步骤S4中,控制晶杆4带动石墨托5远离助溶剂移动的同时带动石墨托5旋转,例如,晶杆4的提拉速度为1-2毫米/小时,并且,控制石墨坩埚3以相反于石墨托5旋转方向的方向旋转,以同时在石墨托5下方的碳膜层6上及石墨坩埚3底壁的碳膜层6上结晶,得到两块n型碳化硅多晶。本实施例中得到的n型碳化硅多晶电阻率低于30mΩ·cm(毫欧姆·厘米)。For example, when making n-type silicon carbide polycrystal, the bottom inner wall of graphite crucible 3 and the bottom surface of graphite holder 5 have carbon film layer 6 respectively, and the manufacture method of silicon carbide polycrystal also comprises filling helium in chamber 1 and nitrogen. It should be noted that nitrogen gas is filled into the chamber 1 at a fixed flow rate, and the main growth atmosphere of silicon carbide polycrystalline is helium gas. The pressure of the gas in the chamber 1 is controlled to be 0.5-1 atmosphere, the co-solvent includes Si element and Cr element, and the temperature of the co-solvent is 2000°C. In step S4, the crystal rod 4 is controlled to drive the graphite holder 5 to move away from the cosolvent while driving the graphite holder 5 to rotate, for example, the pulling speed of the crystal rod 4 is 1-2 mm/hour, and the graphite crucible 3 is controlled to reversely Rotate in the direction of the rotation direction of the graphite holder 5 to simultaneously crystallize on the carbon film layer 6 below the graphite holder 5 and on the carbon film layer 6 on the bottom wall of the graphite crucible 3 to obtain two n-type silicon carbide polycrystals. The n-type silicon carbide polycrystalline resistivity obtained in this embodiment is lower than 30 mΩ·cm (milliohm·cm).
综上可知,通过控制以下三种工艺参数能够控制碳化硅多晶的生长速度和质量。其中,一个工艺参数为晶杆4和坩埚托7中的冷却氦气的流量。一个工艺参数为生长气氛及压强,生长气氛为氦气、氩气、氮气、氢气中的至少一种,压强介于0.2-2个大气压。一个工艺参数为晶杆4的旋转速度、向上提拉速度,以及石墨坩埚3的旋转速度。一个工艺参数为感应加热的功率,以控制助熔剂100的温度。 In summary, it can be seen that the growth rate and quality of silicon carbide polycrystalline can be controlled by controlling the following three process parameters. Wherein, one process parameter is the flow rate of the cooling helium in the crystal rod 4 and the crucible holder 7 . A process parameter is growth atmosphere and pressure. The growth atmosphere is at least one of helium, argon, nitrogen, and hydrogen, and the pressure is between 0.2-2 atmospheres. One process parameter is the rotation speed of the crystal rod 4 , the upward pulling speed, and the rotation speed of the graphite crucible 3 . One process parameter is the power of the induction heating to control the temperature of the flux 100 .

Claims (10)

  1. 一种碳化硅多晶的制造装置,包括:A silicon carbide polycrystalline manufacturing device, comprising:
    腔室(1);chamber(1);
    感应线圈(2),设于所述腔室(1)内;An induction coil (2) is arranged in the chamber (1);
    石墨坩埚(3),设于所述腔室(1)内,且所述石墨坩埚(3)用于容置助溶剂,且所述石墨坩埚(3)的底部内壁能生长碳化硅多晶;A graphite crucible (3) is arranged in the chamber (1), and the graphite crucible (3) is used to accommodate a cosolvent, and the bottom inner wall of the graphite crucible (3) can grow polycrystalline silicon carbide;
    晶杆(4),所述晶杆(4)的一端位于所述石墨坩埚(3)内,所述晶杆(4)的另一端位于所述腔室(1)外;A crystal rod (4), one end of the crystal rod (4) is located in the graphite crucible (3), and the other end of the crystal rod (4) is located outside the chamber (1);
    石墨托(5),固接于所述晶杆(4)的一端,所述石墨托(5)朝向所述石墨坩埚(3)底壁的底面能生长碳化硅多晶。The graphite holder (5) is fixedly connected to one end of the crystal rod (4), and the bottom surface of the graphite holder (5) facing the bottom wall of the graphite crucible (3) can grow polycrystalline silicon carbide.
  2. 根据权利要求1所述的碳化硅多晶的制造装置,还包括碳膜层(6),所述石墨坩埚(3)的底部内壁或所述石墨托(5)的底面中的至少一个具有所述碳膜层(6)。The silicon carbide polycrystalline manufacturing device according to claim 1, further comprising a carbon film layer (6), at least one of the bottom inner wall of the graphite crucible (3) or the bottom surface of the graphite holder (5) has the The carbon film layer (6).
  3. 根据权利要求2所述的碳化硅多晶的制造装置,其中,所述碳膜层(6)的厚度为1~1000微米。The silicon carbide polycrystalline manufacturing device according to claim 2, wherein the carbon film layer (6) has a thickness of 1-1000 microns.
  4. 根据权利要求1-3任一项所述的碳化硅多晶的制造装置,其中,所述晶杆(4)具有第一冷却流道(41),所述第一冷却流道(41)中的冷却流体用于冷却所述石墨托(5)。The silicon carbide polycrystalline manufacturing device according to any one of claims 1-3, wherein the crystal rod (4) has a first cooling flow channel (41), and in the first cooling flow channel (41) The cooling fluid is used to cool the graphite holder (5).
  5. 根据权利要求4所述的碳化硅多晶的制造装置,其中,所述晶杆(4)包括第一管体(42)及套设于所述第一管体(42)外的第二管体(43),所述第二管体(43)固接于所述石墨托(5),所述第一冷却流道(41)包括由所述第一管体(42)形成的第一子流道(411)及由所述第一管体(42)与所述第二管体(43)之间的空隙形成且连通于所述第一子流道(411)的第二子流道(412)。The silicon carbide polycrystalline manufacturing device according to claim 4, wherein the crystal rod (4) comprises a first tube body (42) and a second tube sleeved outside the first tube body (42) body (43), the second tube body (43) is fixed to the graphite holder (5), and the first cooling channel (41) includes a first cooling channel (41) formed by the first tube body (42). The sub-flow channel (411) and the second sub-flow formed by the gap between the first pipe body (42) and the second pipe body (43) and communicated with the first sub-flow channel (411) Road (412).
  6. 根据权利要求1-3任一项所述的碳化硅多晶的制造装置,还包括坩埚托(7),所述坩埚托(7)的一端固接于所述石墨坩埚(3)的底壁,所述坩埚托(7)的另一端位于所述腔室(1)外。The silicon carbide polycrystalline manufacturing device according to any one of claims 1-3, further comprising a crucible holder (7), one end of the crucible holder (7) is affixed to the bottom wall of the graphite crucible (3) , the other end of the crucible holder (7) is located outside the chamber (1).
  7. 根据权利要求6所述的碳化硅多晶的制造装置,其中,所述坩埚托(7)具有第二冷却流道(71),所述第二冷却流道(71)中的冷却流体用于冷却所述石墨坩埚(3)的底壁。The manufacturing device of silicon carbide polycrystal according to claim 6, wherein, the crucible holder (7) has a second cooling channel (71), and the cooling fluid in the second cooling channel (71) is used for Cool the bottom wall of the graphite crucible (3).
  8. 一种碳化硅多晶的制造方法,应用于权利要求1-7任一项所述的碳化硅多晶的制造装置,包括:A silicon carbide polycrystalline manufacturing method, applied to the silicon carbide polycrystalline manufacturing device described in any one of claims 1-7, comprising:
    向石墨坩埚(3)内放入助溶剂;Put into cosolvent in graphite crucible (3);
    通过感应线圈(2)加热所述助溶剂,以使所述助溶剂熔化; heating the co-solvent through an induction coil (2) to melt the co-solvent;
    通过晶杆(4)带动石墨托(5)靠近所述助溶剂移动,以使所述石墨托(5)的下表面与所述助溶剂的液面平齐或间距小于预设间距;The crystal rod (4) drives the graphite support (5) to move close to the co-solvent, so that the lower surface of the graphite support (5) is flush with the liquid level of the co-solvent or the distance is smaller than the preset distance;
    控制所述晶杆(4)带动石墨托(5)远离所述助溶剂移动,以使在所述石墨托(5)下表面形成的碳化硅多晶的底面始终与所述助溶剂的液面平齐或间距小于预设间距。Control the crystal rod (4) to drive the graphite support (5) to move away from the co-solvent, so that the bottom surface of the polycrystalline silicon carbide formed on the lower surface of the graphite support (5) is always in contact with the liquid level of the co-solvent Flush or spaced less than the preset spacing.
  9. 根据权利要求8所述的碳化硅多晶的制造方法,其中,所述碳化硅多晶的制造装置还包括坩埚托(7),所述晶杆(4)具有第一冷却流道(41),所述坩埚托(7)具有第二冷却流道(71);The method for manufacturing polycrystalline silicon carbide according to claim 8, wherein the apparatus for manufacturing polycrystalline silicon carbide further comprises a crucible holder (7), and the crystal rod (4) has a first cooling channel (41) , the crucible holder (7) has a second cooling channel (71);
    还包括:Also includes:
    同时控制所述第一冷却流道(41)和所述第二冷却流道(71)中的冷却流体的流量,从而控制所述石墨托(5)和所述石墨坩埚(3)附近的温度梯度,进而控制碳化硅多晶的生长速度和质量。Simultaneously control the flow of cooling fluid in the first cooling channel (41) and the second cooling channel (71), thereby controlling the temperature near the graphite holder (5) and the graphite crucible (3) Gradient, and then control the growth rate and quality of silicon carbide polycrystalline.
  10. 根据权利要求8所述的碳化硅多晶的制造方法,还包括:The method for manufacturing silicon carbide polycrystalline according to claim 8, further comprising:
    向所述腔室(1)内充入氦气,所述助溶剂包括Si元素、Cr元素和Al元素,在所述石墨托(5)下方的碳膜层(6)上及所述石墨坩埚(3)底壁的碳膜层(6)上结晶,得到两块p型碳化硅多晶;或者Fill helium into the chamber (1), the cosolvent includes Si element, Cr element and Al element, on the carbon film layer (6) below the graphite support (5) and the graphite crucible (3) Crystallization on the carbon film layer (6) of the bottom wall to obtain two p-type silicon carbide polycrystals; or
    向所述腔室(1)内充入氦气及氮气,所述助溶剂包括Si元素和Cr元素,在所述石墨托(5)下方的碳膜层(6)上及所述石墨坩埚(3)底壁的碳膜层(6)上结晶,得到两块n型碳化硅多晶。 Charge helium and nitrogen into the chamber (1), the cosolvent includes Si elements and Cr elements, on the carbon film layer (6) below the graphite holder (5) and the graphite crucible ( 3) Crystallization on the carbon film layer (6) on the bottom wall to obtain two n-type silicon carbide polycrystals.
PCT/CN2023/072842 2022-01-29 2023-01-18 Device and method for manufacturing silicon carbide polycrystal WO2023143297A1 (en)

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CN114481325A (en) * 2022-01-29 2022-05-13 北京青禾晶元半导体科技有限责任公司 Device and method for manufacturing silicon carbide polycrystal
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Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102762780A (en) * 2010-02-18 2012-10-31 丰田自动车株式会社 Method of producing silicon carbide single crystal
CN103620094A (en) * 2011-06-17 2014-03-05 新日铁住金株式会社 Apparatus and method for producing SiC single crystal
CN104695007A (en) * 2013-12-06 2015-06-10 信越化学工业株式会社 Method for growing silicon carbide crystal
CN106048728A (en) * 2016-06-28 2016-10-26 山东天岳晶体材料有限公司 Method for growing high-quality silicon carbide whiskers
CN106884205A (en) * 2015-12-15 2017-06-23 丰田自动车株式会社 SiC monocrystalline and its manufacture method
CN107190322A (en) * 2017-04-01 2017-09-22 中国科学院上海硅酸盐研究所 A kind of growing method of the adjustable carborundum polycrystalline ceramics of large scale resistivity
CN114395799A (en) * 2022-01-29 2022-04-26 北京青禾晶元半导体科技有限责任公司 Device and method for simultaneously manufacturing silicon carbide single crystal and silicon carbide polycrystal
CN114481325A (en) * 2022-01-29 2022-05-13 北京青禾晶元半导体科技有限责任公司 Device and method for manufacturing silicon carbide polycrystal

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013088947A1 (en) * 2011-12-16 2013-06-20 株式会社豊田自動織機 METHOD FOR GROWING SiC CRYSTAL
JP6558394B2 (en) * 2017-04-26 2019-08-14 トヨタ自動車株式会社 Method and apparatus for producing SiC single crystal

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102762780A (en) * 2010-02-18 2012-10-31 丰田自动车株式会社 Method of producing silicon carbide single crystal
CN103620094A (en) * 2011-06-17 2014-03-05 新日铁住金株式会社 Apparatus and method for producing SiC single crystal
CN104695007A (en) * 2013-12-06 2015-06-10 信越化学工业株式会社 Method for growing silicon carbide crystal
CN106884205A (en) * 2015-12-15 2017-06-23 丰田自动车株式会社 SiC monocrystalline and its manufacture method
CN106048728A (en) * 2016-06-28 2016-10-26 山东天岳晶体材料有限公司 Method for growing high-quality silicon carbide whiskers
CN107190322A (en) * 2017-04-01 2017-09-22 中国科学院上海硅酸盐研究所 A kind of growing method of the adjustable carborundum polycrystalline ceramics of large scale resistivity
CN114395799A (en) * 2022-01-29 2022-04-26 北京青禾晶元半导体科技有限责任公司 Device and method for simultaneously manufacturing silicon carbide single crystal and silicon carbide polycrystal
CN114481325A (en) * 2022-01-29 2022-05-13 北京青禾晶元半导体科技有限责任公司 Device and method for manufacturing silicon carbide polycrystal

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