JP2013056807A - METHOD FOR PRODUCING SiC SINGLE CRYSTAL, AND SiC SINGLE CRYSTAL OBTAINED THEREBY - Google Patents

METHOD FOR PRODUCING SiC SINGLE CRYSTAL, AND SiC SINGLE CRYSTAL OBTAINED THEREBY Download PDF

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JP2013056807A
JP2013056807A JP2011196581A JP2011196581A JP2013056807A JP 2013056807 A JP2013056807 A JP 2013056807A JP 2011196581 A JP2011196581 A JP 2011196581A JP 2011196581 A JP2011196581 A JP 2011196581A JP 2013056807 A JP2013056807 A JP 2013056807A
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JP5850490B2 (en
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Takeshi Mitani
武志 三谷
Tetsuo Takahashi
徹夫 高橋
Tomohisa Kato
智久 加藤
Kazuhisa Kurashige
和央 蔵重
Senguttoban Nachimusu
セングットバン ナチムス
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National Institute of Advanced Industrial Science and Technology AIST
Showa Denko Materials Co Ltd
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Hitachi Chemical Co Ltd
National Institute of Advanced Industrial Science and Technology AIST
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Abstract

PROBLEM TO BE SOLVED: To provide production of an SiC single crystal by a solution method capable of suppressing greatly void defects caused by entrainment of bubbles without using a special device, even in a pressurized condition with an atmospheric gas pressure of ≥0.1 MPa at a high temperature that enables SiC solution growth to be executed.SOLUTION: This invention relates to an SiC single crystal in which the void density of a crystal growth portion is ≤10,000/cm, and which is produced by keeping temporarily a solution temperature at a higher temperature by 50-300°C than a crystal growth temperature before dipping a seed crystal into the solution, when dipping the seed crystal of SiC into a solution containing Si and C, and depositing and growing SiC by a solution growth method. A method for producing an SiC single crystal is also provided.

Description

本発明は、溶液法によるSiC(炭化珪素)単結晶の成長方法による製造方法に関し、溶液法による成長結晶中の気泡巻き込みによるボイド欠陥を大幅に抑制することを実現し、かつ表面のモフォロジーの向上を実現するSiC単結晶の製造方法およびこれにより得られる高品質なSiC単結晶に関するものである。   The present invention relates to a method for producing a SiC (silicon carbide) single crystal by a solution method, and realizes a significant suppression of void defects due to entrainment of bubbles in the grown crystal by the solution method, and improves the surface morphology. And a high-quality SiC single crystal obtained thereby.

熱的・化学的安定性に優れたSiC単結晶は、Si(珪素)と比較してバンドギャップエネルギーが約3倍、絶縁破壊電界が7倍、熱伝導率が3倍と大きく、かつ不純物の添加によって伝導型(p型、n型)制御が容易であり、熱酸化膜の形成がSiと同様に可能であることから、Siやガリウムヒ素などの既存技術では達成できない高温、高耐圧、高周波、高耐環境性を有する次世代の電力変換用素子への応用が強く期待されている。   SiC single crystal with excellent thermal and chemical stability has a band gap energy of about 3 times, a dielectric breakdown electric field of 7 times, and a thermal conductivity of 3 times that of Si (silicon). Addition makes it easy to control the conduction type (p-type and n-type) and allows the formation of a thermal oxide film as well as Si. Application to next-generation power conversion elements having high environmental resistance is strongly expected.

SiC単結晶の成長法としては、アチソン法、気相法(昇華法、化学気相法)、溶液法が知られている。アチソン法ではSi原料である硅砂とC(炭素)原料となるコークスを黒鉛電極周囲に配置し、黒鉛電極を通電加熱することにより不定形板状SiC結晶を得る。この際、不純物制御や形状制御が困難であり、半導体基板の作製には向いていない。気相法の代表例である昇華法はインチサイズの単結晶基板が作製可能であるが、結晶中の欠陥密度が大きいという問題がある。化学気相(CVD)法はガスによる原料供給を行うため、一般的には薄膜結晶成長の方法であり、バルク単結晶成長法としては多くの課題を残している。
溶液法は、黒鉛坩堝中でSi又はSi含有合金を融解し、その融液中に黒鉛坩堝もしくは炭化水素ガス供給によって気相からCを溶解させ、低温部に設置した単結晶基板上にSiC結晶層を溶液析出によって成長させる方法である。溶液法は気相法に比べ比較的熱平衡状態に近い条件で結晶成長が進行すると考えられることから、一般的には高品質な単結晶を得る方法としては好都合であることが知られている。上述の理由から、近年、溶液法によるSiC単結晶の成長方法について、成長速度や結晶品質を高める検討がなされている。
As an SiC single crystal growth method, an Atchison method, a vapor phase method (sublimation method, chemical vapor phase method), or a solution method is known. In the Atchison method, cinnabar sand, which is a Si raw material, and coke, which is a C (carbon) raw material, are arranged around a graphite electrode, and an amorphous plate-like SiC crystal is obtained by energizing and heating the graphite electrode. At this time, impurity control and shape control are difficult and are not suitable for manufacturing a semiconductor substrate. The sublimation method, which is a typical example of the vapor phase method, can produce an inch-size single crystal substrate, but has a problem that the defect density in the crystal is large. The chemical vapor deposition (CVD) method is generally a thin film crystal growth method because it supplies a raw material by gas, and many problems remain as a bulk single crystal growth method.
In the solution method, Si or a Si-containing alloy is melted in a graphite crucible, C is dissolved in the melt from a gas phase by supplying the graphite crucible or a hydrocarbon gas, and a SiC crystal is formed on a single crystal substrate placed in a low temperature part. It is a method of growing a layer by solution deposition. It is known that the solution method is generally advantageous as a method for obtaining a high-quality single crystal because crystal growth is considered to proceed under conditions that are relatively close to a thermal equilibrium state as compared with a gas phase method. For the reasons described above, in recent years, studies have been made on increasing the growth rate and crystal quality of a method for growing a SiC single crystal by a solution method.

特許文献1には、Si及びC、またはSi、Cr及びM(M:Ti、Fe、Mn、Coのいずれか一種以上)からなる、SiCが溶解している融液中に、SiCの種結晶基板を浸漬し、少なくとも種結晶基板周辺における溶液過冷却によりSiCを過飽和状態とすることによって、種結晶基板上にSiC単結晶を成長させる方法において、気泡を含まない良質なバルクSiC単結晶を、2000℃以下の温度で実用的な成長速度で安定して製造する方法が提案され、単結晶成長時の雰囲気ガスとして、単結晶成長温度での粘度ηが750μP以下の非酸化性ガス、例えばヘリウムまたはヘリウムを主成分とする混合ガスを使用することによって、成長結晶中の気泡発生を完全に抑制することができると記述されている。
しかしながら、不純物元素の少ない高品質で、高い成長速度で結晶成長を実施するためには、Si及びCの2元系溶液を用い、かつ2000℃以上の高温下で成長することが望まれる。この場合、Si溶液の蒸発を防ぐために雰囲気ガスを加圧する方法がとられる。発明者らが実験を行ったところ、結晶成長温度2100℃、雰囲気ガス(He)0.95MPaの結晶成長条件において、気泡の巻き込みを抑制することはできなかった。
Patent Document 1 discloses a SiC seed crystal in a melt containing SiC, which is made of Si and C, or Si, Cr, and M (M: any one of Ti, Fe, Mn, and Co). In a method of growing a SiC single crystal on a seed crystal substrate by immersing the substrate and supersaturating SiC by solution supercooling at least around the seed crystal substrate, a high-quality bulk SiC single crystal that does not contain bubbles, A method of stably producing at a practical growth rate at a temperature of 2000 ° C. or less has been proposed. As an atmospheric gas during single crystal growth, a non-oxidizing gas having a viscosity η of 750 μP or less at the single crystal growth temperature, for example, helium Alternatively, it is described that the generation of bubbles in the grown crystal can be completely suppressed by using a mixed gas containing helium as a main component.
However, in order to perform crystal growth at a high quality with a small amount of impurity elements and at a high growth rate, it is desired to use a binary solution of Si and C and grow at a high temperature of 2000 ° C. or higher. In this case, a method of pressurizing the atmospheric gas is used to prevent evaporation of the Si solution. As a result of an experiment conducted by the inventors, it was not possible to suppress entrainment of bubbles under the crystal growth conditions of a crystal growth temperature of 2100 ° C. and an atmospheric gas (He) of 0.95 MPa.

非特許文献1には、結晶成長温度T≦2300℃、圧力P≦20MPaの結晶成長条件において、Ar雰囲気ガス下で、Si及びCの2元系溶液で数10〜100μm/hの速度で結晶成長が行われている。しかしながら、該非特許文献1には、使用するArガスの巻き込みや溶液の巻き込みなどが不可避に生じると記述されている。   Non-Patent Document 1 discloses that crystals are grown at a rate of several tens to 100 μm / h in a binary solution of Si and C under Ar atmosphere gas under crystal growth conditions of crystal growth temperature T ≦ 2300 ° C. and pressure P ≦ 20 MPa. Growth is taking place. However, Non-Patent Document 1 describes that the use of Ar gas to be used or the solution is inevitably involved.

特許文献2には、黒鉛坩堝内で加熱されたSiを融解した溶液にSiC単結晶を接触させ基板上にSiC単結晶を成長させる方法において、融液内にCrおよびX(XはCe、Ndのうち少なくともいずれか1種以上である)の元素を全組成中の各々の元素の割合としてCrが30〜70at.%であってかつ、1)XがCeである場合はCeが0.5〜20at.%、2)XがNdである場合はNdを1〜25at.%である融液で、SiC単結晶を析出成長させる方法が提案されている。
しかしながら、該特許文献2に記載の技術は、融液組成が限定されており、これ以外の融液組成を用いた場合には、SiC単結晶の溶液成長に対して汎用的に効果を発揮するとは限らない。
In Patent Document 2, in a method in which a SiC single crystal is grown on a substrate by bringing a SiC single crystal into contact with a solution obtained by melting Si heated in a graphite crucible, Cr and X (X is Ce, Nd) in the melt. At least one of them), and Cr is 30 to 70 at. %, And 1) when X is Ce, Ce is 0.5 to 20 at. %, 2) When X is Nd, Nd is 1 to 25 at. A method of precipitating and growing SiC single crystals with a melt of% is proposed.
However, the technique described in Patent Document 2 has a limited melt composition, and when a melt composition other than this is used, the technique is generally effective for solution growth of SiC single crystals. Is not limited.

特許文献3には、溶液法を用いたSiC単結晶の析出・成長方法において、溶液界面の面積(Ss)に対するSiC種結晶の表面積(Sc)の割合(Sc/Ss)を0.13以下、結晶成長開始前の坩堝内の雰囲気圧力を55kPa以上とし、結晶成長開始以後の坩堝内の雰囲気圧力を150kPa以下とすることにより、SiC単結晶中の多結晶の混入確率を低減するとともに単結晶中のボイド密度を低減し得るSiC単結晶の製造方法が記載されている。
しかしながら、該特許文献3に記載の技術は、ボイド欠陥の完全な抑制は達成できておらず、且つ、溶液界面の面積(Ss)に対するSiC種結晶の表面積(Sc)の割合(Sc/Ss)を0.01〜0.13にする必要があることから、結晶の成長に用いる種結晶の直径よりも7〜100倍大きな直径の坩堝を用いなくてはならず、装置の大型化が必要であり、工業生産上は問題がある。また、不純物元素の少ない高品質で、高い成長速度で結晶成長を実施するためには、Si及びCの2元系溶液を用い、かつ2000℃以上の高温下の条件が望まれる。この場合、該特許文献3に記載の方法ではSi溶液の蒸発が顕著であり、2100℃を超える温度では実施が困難である。
In Patent Document 3, in the SiC single crystal precipitation / growth method using the solution method, the ratio (Sc / Ss) of the surface area (Sc) of the SiC seed crystal to the area (Ss) of the solution interface is 0.13 or less. By setting the atmospheric pressure in the crucible before the start of crystal growth to 55 kPa or more and the atmospheric pressure in the crucible after the start of crystal growth to 150 kPa or less, the mixing probability of polycrystals in the SiC single crystal is reduced and the single crystal is A method for producing an SiC single crystal that can reduce the void density of the metal is described.
However, the technique described in Patent Document 3 does not achieve complete suppression of void defects, and the ratio of the surface area (Sc) of the SiC seed crystal to the area (Ss) of the solution interface (Sc / Ss). Therefore, it is necessary to use a crucible having a diameter 7 to 100 times larger than the diameter of the seed crystal used for crystal growth, and it is necessary to increase the size of the apparatus. There is a problem in industrial production. In addition, in order to perform crystal growth at a high quality with a small amount of impurity elements and at a high growth rate, it is desirable to use a binary solution of Si and C and to be at a high temperature of 2000 ° C. or higher. In this case, in the method described in Patent Document 3, the evaporation of the Si solution is remarkable, and it is difficult to carry out at a temperature exceeding 2100 ° C.

特開2006−69861号公報JP 2006-69861 A 特許第4450075号公報Japanese Patent No. 4450075 特開2011−68515号公報JP 2011-68515 A

Material Science Engineering,B61−62,(1999)29−39Material Science Engineering, B61-62, (1999) 29-39.

以上のように、前述の公知文献における溶液法によるSiC単結晶の成長法は、2000℃以下の条件で、雰囲気ガス粘度が750μP以下となる非酸化性ガス(例えばHe)を用いる方法であるが、特定の溶液組成における成長結晶中のマクロ欠陥の低減効果について記載されているものの、SiC単結晶を成長し得る全ての成長温度(特に2000℃以上)や溶液組成に対して、ボイドを抑制し得る有効な方法ではなかった。また、雰囲気ガスの圧力制御および坩堝・種結晶の構造を制御することによってボイド低減及び多結晶抑制を実現する方法も記載されているが、そのボイド抑制効果は完全ではなく、また、作製する単結晶よりも7〜100倍の直径を持つ大きな坩堝を用いなくてはならず、装置の大型化が必要であり、工業生産上は問題がある。また、高品質高純度のSiC単結晶の作製のためには、Siのみを溶液として用いることが望ましく、これらの公知文献に記載の方法では、Siのみを溶液として用いた場合に、成長結晶中のマクロ欠陥を抑制し、成長結晶表面モフォロジーの向上を実現することは困難である。
本発明は、雰囲気ガスの種類、雰囲気ガスの圧力、SiとCを含む溶液への遷移金属元素または/および希土類元素の添加の有無を問わず、SiC溶液成長法が実施可能な結晶成長温度において、溶液成長法では典型的に発生するボイド欠陥を大幅に抑制することが可能であるSiC単結晶の成長方法を提供することを目的とする。
As described above, the SiC single crystal growth method by the solution method in the above-mentioned known literature is a method using a non-oxidizing gas (for example, He) having an atmospheric gas viscosity of 750 μP or less under conditions of 2000 ° C. or less. Although it describes the effect of reducing macro defects in grown crystals in a specific solution composition, it suppresses voids against all growth temperatures (particularly 2000 ° C. or higher) and solution compositions capable of growing SiC single crystals. It was not an effective way to get. Although a method for realizing void reduction and polycrystal suppression by controlling the pressure of the atmospheric gas and the structure of the crucible / seed crystal is also described, the effect of suppressing the void is not perfect, and the simple manufacturing method is not limited. A large crucible having a diameter 7 to 100 times larger than that of the crystal must be used, and the apparatus must be increased in size, which is problematic in industrial production. In addition, it is desirable to use only Si as a solution for the production of a high-quality, high-purity SiC single crystal. In the methods described in these known documents, when only Si is used as a solution, It is difficult to suppress the macro defects and to improve the growth crystal surface morphology.
The present invention provides a crystal growth temperature at which the SiC solution growth method can be performed regardless of the type of atmospheric gas, the pressure of the atmospheric gas, and whether or not a transition metal element and / or rare earth element is added to a solution containing Si and C. An object of the present invention is to provide a method for growing a SiC single crystal that can significantly suppress void defects typically generated in the solution growth method.

本発明者等は、溶液法によるSiC単結晶の製造方法について検討を行った結果、SiC単結晶中のボイドは、溶液に溶け込んだ雰囲気ガスが再びガス化し気泡を発生し、その気泡が結晶成長とともに取り込まれることが原因の一つであることを見出し、加えて、溶液温度の調整によって、雰囲気ガスの溶液に対する溶解度を制御することが可能であることを見出した。これらの新たな知見により、ボイドの原因となる気泡を取り除く方法を更に鋭意検討し、種結晶を溶液に浸漬する前の段階での処理条件が重要であることを明らかにし、本発明に至った。
本発明の課題は、以下の手段によって達成された。
(1)Si及びCを含む溶液中に、SiCの種結晶を浸漬し、溶液成長法によりSiCを析出・成長させるにあたり、該種結晶を該溶液に浸漬する前に、該溶液の温度を一時的に結晶成長温度よりも50〜300℃高温に保って製造して、結晶成長部分のボイド密度を10000個/cm以下としたことを特徴とするSiC単結晶。
(2)Si及びCを含む溶液中に、SiCの種結晶を浸漬し、SiCを析出・成長させる溶液成長法によるSiC単結晶の製造方法であって、該種結晶を該溶液に浸漬する前に、該溶液の温度を一時的に結晶成長温度よりも50〜300℃高温に保つことを特徴とするSiC単結晶の製造方法。
(3)前記溶液の温度を一時的に前記結晶成長温度よりも高温に保つ時間が10分以上、3時間以下であることを特徴とする(2)に記載のSiC単結晶の製造方法。
(4)前記SiC単結晶の製造をガス雰囲気下で行い、該雰囲気ガスの圧力が0.1MPa以上の加圧条件に設定されていることを特徴とする(2)または(3)に記載のSiC単結晶の製造方法。
(5)前記結晶成長温度が、1700〜2100℃の範囲内であることを特徴とする(2)〜(4)のいずれか1項に記載のSiC単結晶の製造方法。
(6)前記溶液中に遷移金属元素および/または希土類元素を含むことを特徴とする(2)〜(5)のいずれかに記載のSiC単結晶の製造方法。
(7)前記(2)〜(6)のいずれか1項に記載の製造方法で製造されたSiC単結晶。
As a result of studying the manufacturing method of the SiC single crystal by the solution method, the present inventors found that the voids in the SiC single crystal were gasified again from the atmospheric gas dissolved in the solution, and the bubbles were crystal-grown. In addition, it was found that it is one of the causes, and in addition, it was found that the solubility of the atmospheric gas in the solution can be controlled by adjusting the solution temperature. Based on these new findings, the method for removing bubbles that cause voids has been further studied, and it has been clarified that the treatment conditions before the seed crystal is immersed in the solution are important, leading to the present invention. .
The object of the present invention has been achieved by the following means.
(1) In immersing a SiC seed crystal in a solution containing Si and C, and precipitating and growing SiC by the solution growth method, the temperature of the solution is temporarily set before immersing the seed crystal in the solution. In particular, the SiC single crystal is manufactured by maintaining the crystal growth temperature at 50 to 300 ° C. higher than the crystal growth temperature, and the void density in the crystal growth portion is set to 10,000 pieces / cm 3 or less.
(2) A method for producing a SiC single crystal by a solution growth method in which a SiC seed crystal is immersed in a solution containing Si and C, and SiC is precipitated and grown, before the seed crystal is immersed in the solution. And a temperature of the solution is temporarily maintained at 50 to 300 ° C. higher than the crystal growth temperature.
(3) The method for producing an SiC single crystal according to (2), wherein the time for keeping the temperature of the solution temporarily higher than the crystal growth temperature is 10 minutes or more and 3 hours or less.
(4) The SiC single crystal is manufactured under a gas atmosphere, and the pressure of the atmosphere gas is set to a pressurizing condition of 0.1 MPa or more. (2) or (3) A method for producing a SiC single crystal.
(5) The method for producing an SiC single crystal according to any one of (2) to (4), wherein the crystal growth temperature is in a range of 1700 to 2100 ° C.
(6) The method for producing a SiC single crystal according to any one of (2) to (5), wherein the solution contains a transition metal element and / or a rare earth element.
(7) A SiC single crystal manufactured by the manufacturing method according to any one of (2) to (6).

本発明により、SiC単結晶の溶液成長が実施可能な高温で、雰囲気ガス圧力が0.1MPa以上の加圧条件においても、特別な装置を用いることなく、雰囲気ガスの気泡の巻き込みによるボイド欠陥が低減されたSiC単結晶およびその製造方法を提供することができる。   According to the present invention, void defects due to entrainment of atmospheric gas bubbles can be achieved without using a special apparatus even at high temperature at which the solution growth of the SiC single crystal can be carried out and under a pressurized condition where the atmospheric gas pressure is 0.1 MPa or more. A reduced SiC single crystal and a method for producing the same can be provided.

図1は本発明の実施例において用いた溶液法によるSiC単結晶成長実験装置の模式図である。FIG. 1 is a schematic diagram of a SiC single crystal growth experimental apparatus by a solution method used in an example of the present invention. 図2は実施例1〜3で結晶成長開始前に溶液を高温処理した結晶成長実験における溶液温度の時間変化を示すグラフであり、結晶成長開始前に溶液を1900℃の結晶成長温度よりも200℃高い、2100℃に保持した。FIG. 2 is a graph showing the time change of the solution temperature in a crystal growth experiment in which the solution was treated at a high temperature before the start of crystal growth in Examples 1 to 3, and the solution was changed from the crystal growth temperature of 1900 ° C. to 200 ° C. before the start of crystal growth. The temperature was kept at 2100 ° C., which was higher. 図3は比較例1で結晶成長開始前に溶液を高温処理しない結晶成長実験における溶液温度の時間変化を示すグラフであり、結晶成長温度は1900℃である。FIG. 3 is a graph showing the change over time of the solution temperature in a crystal growth experiment in which the solution is not treated at a high temperature before the start of crystal growth in Comparative Example 1, and the crystal growth temperature is 1900 ° C. 図4は比較例2で結晶成長開始前に溶液を高温処理しない結晶成長実験における溶液温度の時間変化を示すグラフであり、結晶成長温度は2100℃である。FIG. 4 is a graph showing the change over time of the solution temperature in a crystal growth experiment in which the solution is not treated at a high temperature before the start of crystal growth in Comparative Example 2, and the crystal growth temperature is 2100 ° C. 図5は実施例1で得られたSiC単結晶の成長面および成長面に垂直な断面の透過画像を示す光学顕微鏡写真である。FIG. 5 is an optical micrograph showing a growth surface of the SiC single crystal obtained in Example 1 and a transmission image of a cross section perpendicular to the growth surface. 図6は比較例1で得られたSiC単結晶の成長面および成長面に垂直な断面の透過画像を示す光学顕微鏡写真である。FIG. 6 is an optical micrograph showing a growth surface of the SiC single crystal obtained in Comparative Example 1 and a transmission image of a cross section perpendicular to the growth surface.

本発明のSiC単結晶の製造方法は、溶液法によりSiC単結晶を成長させる際、種結晶を溶液に浸漬する前に、溶液の高温処理を行うものであり、溶液の温度を一時的に結晶成長温度よりも50〜300℃高温に保つことにより、1700〜2100℃の高い結晶成長温度で、且つ雰囲気ガス圧力が0.1MPa以上の加圧条件下であっても、特別な装置を用いることなく、結晶成長したSiC結晶中のボイド発生を抑制できる。   The method for producing a SiC single crystal according to the present invention is a method in which when a SiC single crystal is grown by a solution method, a high temperature treatment of the solution is performed before the seed crystal is immersed in the solution. By using a high temperature of 1700 to 2100 ° C. by maintaining the temperature 50 to 300 ° C. higher than the growth temperature and using a special apparatus even under a pressurized condition where the atmospheric gas pressure is 0.1 MPa or more. In addition, generation of voids in the grown SiC crystal can be suppressed.

種結晶を溶液に浸漬する前に、溶液の温度を一時的に成長温度よりも高温に保つことによってボイド発生を抑制した状態でSiC単結晶の作製が可能とするものであるが、結晶成長前の保持温度が結晶成長温度+50℃未満であると、気泡発生の抑制効果が十分ではなく、結晶成長温度+300℃を超えると、溶液中のCの過飽和濃度が高くなりすぎ、多結晶の発生が起こってしまうため、溶液の温度を一時的に成長温度よりも50〜300℃高温に保つことが適正である。また、抑制効果を十分にかつ溶液中のCの過飽和濃度が高くなりすぎないようにするためには、さらに好ましくは、高温保持時間が10分以上、3時間以下であることが望ましい。   Before immersing the seed crystal in the solution, the temperature of the solution is temporarily kept higher than the growth temperature, thereby making it possible to produce a SiC single crystal in a state in which void generation is suppressed. If the holding temperature is less than the crystal growth temperature + 50 ° C., the effect of suppressing bubble generation is not sufficient, and if the crystal growth temperature exceeds + 300 ° C., the supersaturated concentration of C in the solution becomes too high, and polycrystals are generated Therefore, it is appropriate to temporarily maintain the temperature of the solution at 50 to 300 ° C. higher than the growth temperature. Further, in order to obtain a sufficient suppression effect and prevent the supersaturated concentration of C in the solution from becoming too high, it is more preferable that the high temperature holding time is 10 minutes or more and 3 hours or less.

本発明のSiC単結晶の製造方法を実施するための形態の1例を示した図1を用いて説明する。
本発明においては、種結晶を溶液に浸漬する前に、溶液の温度を一時的に結晶成長温度よりも50〜300℃高温に保つことを特徴とする溶液の高温処理を付与する。
種結晶を溶液に浸漬する前に行う溶液の高温処理の温度は、結晶成長温度よりも100〜250℃高いことがより好ましい。
種結晶を溶液に浸漬する前に行う溶液の高温処理の処理時間は、溶液温度が結晶成長温度よりも50〜300℃高温に達すれば、特に限定されるものではないが、好ましくは10分〜3時間、より好ましくは30分〜2時間である。
A description will be given with reference to FIG. 1 showing an example of an embodiment for carrying out the method for producing a SiC single crystal of the present invention.
In the present invention, before immersing the seed crystal in the solution, a high temperature treatment of the solution characterized by temporarily maintaining the temperature of the solution at 50 to 300 ° C. higher than the crystal growth temperature is applied.
The temperature of the high-temperature treatment of the solution performed before immersing the seed crystal in the solution is more preferably 100 to 250 ° C. higher than the crystal growth temperature.
The treatment time of the high temperature treatment of the solution performed before immersing the seed crystal in the solution is not particularly limited as long as the solution temperature reaches 50 to 300 ° C. higher than the crystal growth temperature, but preferably 10 minutes to 3 hours, more preferably 30 minutes to 2 hours.

図1において、SiC単結晶2の成長は、加熱装置である高周波コイル6によって加熱された溶液4に、SiC単結晶基板2を支持する機構の一部である種結晶保持軸(種結晶保持棒)3の先端に、種結晶であるSiCからなる単結晶基板2を接着又は機械的固定により保持し、これを溶液内に浸漬させて単結晶成長させることができる。種結晶保持軸3と黒鉛坩堝1はおのおの独立に回転する機構を備えたものである。黒鉛坩堝1の外側底面の温度は、放射温度計のような高温温度計により直接測温する。高周波コイル6による黒鉛坩堝1の加熱は、黒鉛坩堝1の外側底面の測定温度をもとに制御されるのが好ましい。ここで、図1では、黒鉛坩堝1は断熱材5で覆われ、この外側に高周波コイル6が設置されている。   In FIG. 1, the growth of the SiC single crystal 2 is performed by using a seed crystal holding shaft (seed crystal holding rod) which is a part of a mechanism for supporting the SiC single crystal substrate 2 in a solution 4 heated by a high-frequency coil 6 serving as a heating device. ) A single crystal substrate 2 made of SiC, which is a seed crystal, is held at the tip of 3 by adhesion or mechanical fixation, and this can be immersed in a solution to grow a single crystal. The seed crystal holding shaft 3 and the graphite crucible 1 are each provided with a mechanism that rotates independently. The temperature of the outer bottom surface of the graphite crucible 1 is directly measured by a high temperature thermometer such as a radiation thermometer. The heating of the graphite crucible 1 by the high-frequency coil 6 is preferably controlled based on the measured temperature on the outer bottom surface of the graphite crucible 1. Here, in FIG. 1, the graphite crucible 1 is covered with a heat insulating material 5, and a high-frequency coil 6 is installed on the outside thereof.

種結晶の形状は円盤、六角形平板、四角形平板等の板状でも、立方体でもよいが、円盤、六角形平板、四角形平板等の板状が好ましい。種結晶の大きさは、どのような大きさでもよく、その目的にもよるが、直径0.1cm以上が好ましく、0.5cm以上がより好ましく、1cm以上がさらに好ましい。直径の好ましい上限は特に限定されるものでなく、結晶成長装置の容量に合わせて調製すればよく、例えば10cmでも構わない。   The shape of the seed crystal may be a plate such as a disk, a hexagonal flat plate, or a rectangular flat plate, or a cube, but a plate shape such as a disc, a hexagonal flat plate, or a square flat plate is preferred. The size of the seed crystal may be any size, and depending on the purpose, the diameter is preferably 0.1 cm or more, more preferably 0.5 cm or more, and even more preferably 1 cm or more. The upper limit of the diameter is not particularly limited, and may be adjusted according to the capacity of the crystal growth apparatus, and may be 10 cm, for example.

本発明のSiC単結晶を得る方法において、溶液成長に用いる溶液の組成に関しては、少なくともSiとCが含まれているならば特に制限は無い。本発明においては、溶液成長に用いる溶液には遷移金属元素(好ましくはTi、Cr等の第一遷移元素)または/および希土類元素(例えば、スカンジウム、イットリウム等)を含んでもよい。特に、Si−C溶液、Si−C−Ti溶液、Si−C−Cr溶液が好ましく、溶液に遷移金属元素(好ましくはTi、Cr等の第一遷移元素)または/および希土類元素を含んだ場合においても、種結晶を溶液に浸漬する前に、溶液の温度を一時的に成長温度よりも50〜300℃高温に保つことで、結晶成長して得られたSiC単結晶内のボイドは大幅に抑制される。ここで、Si−C溶液、Si−C−Ti溶液、Si−C−Cr溶液におけるCの少なくとも一部は黒鉛坩堝から溶液中に溶解させたものである。また、Cの一部はCHなどの炭化水素ガスを溶液中に吹き込む、又は雰囲気ガスに混入することにより溶液中にCを供給する方法もある。 In the method for obtaining a SiC single crystal of the present invention, the composition of the solution used for solution growth is not particularly limited as long as at least Si and C are contained. In the present invention, the solution used for solution growth may contain a transition metal element (preferably a first transition element such as Ti or Cr) and / or a rare earth element (for example, scandium or yttrium). In particular, a Si-C solution, a Si-C-Ti solution, or a Si-C-Cr solution is preferable, and the solution contains a transition metal element (preferably a first transition element such as Ti or Cr) or / and a rare earth element. However, before immersing the seed crystal in the solution, by temporarily maintaining the temperature of the solution at 50 to 300 ° C. higher than the growth temperature, voids in the SiC single crystal obtained by crystal growth are greatly increased. It is suppressed. Here, at least a part of C in the Si-C solution, Si-C-Ti solution, and Si-C-Cr solution is dissolved in the solution from the graphite crucible. In addition, there is a method in which a part of C is supplied into the solution by injecting a hydrocarbon gas such as CH 4 into the solution or by mixing it with an atmospheric gas.

雰囲気ガスは、SiC単結晶成長時に、SiC結晶及び溶液の酸化を防止するために、He、Ne、Ar等の不活性ガスを用い、またN、H、CHなどのガスを混合してもよい。また、SiC結晶成長は1700〜2400℃の高温で実施するため、雰囲気ガス圧力が0.1MPaよりも低いと溶液の蒸発が激しいので、加圧条件でSiC単結晶成長を実施することが望ましい。好適な雰囲気ガス圧力は0.1MPa以上である。 As the atmospheric gas, an inert gas such as He, Ne, or Ar is used to prevent oxidation of the SiC crystal and the solution during the growth of the SiC single crystal, and a gas such as N 2 , H 2 , or CH 4 is mixed. May be. Further, since the SiC crystal growth is performed at a high temperature of 1700 to 2400 ° C., the evaporation of the solution is severe when the atmospheric gas pressure is lower than 0.1 MPa. Therefore, it is desirable to perform the SiC single crystal growth under a pressurized condition. A suitable atmospheric gas pressure is 0.1 MPa or more.

本発明の製造方法におけるよるSiC単結晶成長時の温度は、1700〜2100℃の範囲内で設定可能であるが、溶液組成によって最適な温度条件を1700〜2100℃の範囲内で任意に設定すればよい。ただし結晶成長あるいは溶液を高温に保つ場合の温度によっては溶液の蒸発が激しくなるので、雰囲気ガスの圧力としては、1700〜1900℃の溶液温度の場合には0.1MPa〜1MPa、1900℃より高く、2400℃以下の範囲の溶液温度では1MPa〜10MPaが好適である。
本発明における溶液法によるSiC単結晶成長によって、高温で長時間、例えば3時間以上、成長して得られるSiC単結晶中のボイド発生を大幅に抑制することができる。
すなわち、Si及びCを含む溶液中に、SiCの種結晶を浸漬し、SiCを析出・成長させるにあたり、Si及びCを含む溶液中に、SiCの種結晶を浸漬し、SiCを析出・成長させるにあたり、該種結晶を該溶液に浸漬する前に、該溶液の温度を一時的に結晶成長温度よりも50〜300℃高温に保って製造することで得られるSiC単結晶はボイド密度を10000個/cm以下とすることができる。ボイド密度は、好ましくは1000個/cm以下、さらに好ましくは100個/cm以下である。これにより、ボイドの発生で問題とする直径1μm以上のボイドの発生は大幅に抑制でき、実質0個/cmにもできる。
The temperature at the time of SiC single crystal growth by the production method of the present invention can be set within a range of 1700 to 2100 ° C., but an optimum temperature condition can be arbitrarily set within a range of 1700 to 2100 ° C. depending on the solution composition. That's fine. However, since the evaporation of the solution becomes severe depending on the temperature when crystal growth or the solution is kept at a high temperature, the pressure of the atmospheric gas is higher than 0.1 MPa to 1 MPa and 1900 ° C. at a solution temperature of 1700 to 1900 ° C. A solution temperature in the range of 2400 ° C. or lower is preferably 1 MPa to 10 MPa.
By the SiC single crystal growth by the solution method in the present invention, generation of voids in the SiC single crystal obtained by growing at a high temperature for a long time, for example, 3 hours or more can be significantly suppressed.
That is, in immersing a SiC seed crystal in a solution containing Si and C, and precipitating and growing SiC, the SiC seed crystal is immersed in a solution containing Si and C, and SiC is precipitated and grown. In this case, before immersing the seed crystal in the solution, the SiC single crystal obtained by temporarily maintaining the temperature of the solution at 50 to 300 ° C. higher than the crystal growth temperature has a void density of 10,000 pieces. / Cm 3 or less. The void density is preferably 1000 / cm 3 or less, more preferably 100 / cm 3 or less. Thereby, generation | occurrence | production of the void of diameter 1 micrometer or more which is a problem by generation | occurrence | production of a void can be suppressed significantly, and it can also be substantially 0 piece / cm < 3 >.

ボイド密度は、以下のようにして測定できる。
すなわち、光学顕微鏡を用い、透過照明によって、結晶成長部分の厚み方向にすべて含んだ領域にてボイド数を計測する。ここで、ボイドは透過照明で黒丸点として観測されるので、容易に計測できる。また、光学可能顕微鏡観察の空間分解能は1μm程度であり、問題とする1μm以上の大きさのボイドは十分に検出できる。より具体的には、結晶成長部分の平面の2mm×2mmの領域で、結晶成長部分の全厚み(例えば結晶成長した厚みが100μmの場合であれば100μm)の領域を、顕微鏡観察してボイド数計測を行い、それを任意の場所で計6回繰り返し、1cm当たりに換算してその平均値を求める。以後の実施例、比較例はこのようにして求めたものである。なお、ここで、透過照明で全厚みを観察できない厚みの場合は、厚み方向に分割して計測を繰り返すことで計測することができる。
The void density can be measured as follows.
That is, using an optical microscope, the number of voids is measured in a region including all of the crystal growth portion in the thickness direction by transmission illumination. Here, since the void is observed as a black dot by transmitted illumination, it can be easily measured. In addition, the spatial resolution of observation with an optical microscope is about 1 μm, and a void having a size of 1 μm or more in question can be sufficiently detected. More specifically, in a 2 mm × 2 mm region on the plane of the crystal growth portion, the total thickness of the crystal growth portion (for example, 100 μm if the crystal growth thickness is 100 μm) is observed with a microscope and the number of voids Measurement is performed, and the measurement is repeated a total of 6 times at an arbitrary place, and the average value is obtained by converting per 1 cm 3 . The following examples and comparative examples were obtained in this way. Here, when the thickness cannot be observed with the transmitted illumination, the thickness can be measured by dividing in the thickness direction and repeating the measurement.

以下に、本発明を具体的に説明する目的で実施例を示す。ただし、これらの実施例は、本発明の具体的説明を目的としており、本発明を制限する意図はない。
以下の実施例では、図1に示したSiC単結晶成長の実施形態と同様の装置を用いて、SiC単結晶の成長を行った。実験では、溶液にはSiを用い、結晶成長温度1900℃、雰囲気ガス圧力0.95MPaとした。種結晶を溶液に浸漬する前に、高温処理として、溶液の温度を結晶成長温度よりも200℃高温に1時間保持した。ここで使用した種結晶は、2.5〜5.1cmの大きさの板状のSiC単結晶基板を使用した。
Examples are given below for the purpose of specifically explaining the present invention. However, these examples are for the purpose of illustrating the present invention and are not intended to limit the present invention.
In the following examples, a SiC single crystal was grown using the same apparatus as that of the SiC single crystal growth embodiment shown in FIG. In the experiment, Si was used as the solution, the crystal growth temperature was 1900 ° C., and the atmospheric gas pressure was 0.95 MPa. Before immersing the seed crystal in the solution, as a high temperature treatment, the temperature of the solution was maintained at 200 ° C. higher than the crystal growth temperature for 1 hour. The seed crystal used here was a plate-like SiC single crystal substrate having a size of 2.5 to 5.1 cm.

実験では、黒鉛坩堝にSiを充填し、減圧下でSiの融点以下の温度に保持して吸着ガスを脱気した後、雰囲気ガスとしてArガスを0.95MPaの圧力で充填し、黒鉛坩堝の底面が所定の温度になるように加熱し、Si原料を融解させた。その後、溶液の温度を成長温度よりも200℃上昇させた状態で1時間保持し、その後に結晶成長温度まで温度を降下させた。その後、図1に例示した種結晶保持軸と同様な構造によって保持されたSiC種結晶を溶液に浸漬し、3時間の浸漬時間が経過した後、種結晶保持軸を上昇させ、種結晶を溶液から引き揚げた。結晶成長中は種結晶保持軸と黒鉛坩堝を互いに逆方向に回転させた。   In the experiment, the graphite crucible was filled with Si, held at a temperature below the melting point of Si under reduced pressure, and the adsorbed gas was degassed, and then filled with Ar gas at a pressure of 0.95 MPa as the atmospheric gas, The Si raw material was melted by heating so that the bottom surface had a predetermined temperature. Thereafter, the temperature of the solution was maintained for 1 hour in a state of 200 ° C. higher than the growth temperature, and then the temperature was lowered to the crystal growth temperature. Thereafter, the SiC seed crystal held by the same structure as the seed crystal holding shaft illustrated in FIG. 1 is immersed in the solution, and after the immersion time of 3 hours has elapsed, the seed crystal holding shaft is raised, Pulled from. During crystal growth, the seed crystal holding shaft and the graphite crucible were rotated in opposite directions.

炉内の温度を室温まで冷却させた後、SiC種結晶を回収し、フッ硝酸を用いて洗浄を行い、SiC結晶表面に付着している溶液の凝固物を取り除いた。種結晶上に溶液法により成長したSiC単結晶の表面と断面に対して、透過照明を用いた顕微鏡観察を実施し、成長結晶中のボイド密度を前述のようにして計測した。   After the temperature in the furnace was cooled to room temperature, the SiC seed crystal was recovered and washed with hydrofluoric acid to remove the solidified product of the solution adhering to the SiC crystal surface. The surface and cross section of the SiC single crystal grown by the solution method on the seed crystal was observed with a microscope using transmitted illumination, and the void density in the grown crystal was measured as described above.

(実施例1)
実験では、黒鉛坩堝にSiを充填し、1Pa以下の減圧下で黒鉛坩堝及びSi原料を1100℃程度の温度に保持し、吸着ガスを脱気した後、雰囲気ガスとしてArガスを0.95MPaの圧力になるように充填し、黒鉛坩堝の底面が1900℃になるように加熱し、Si原料を融解させた。その後、溶液の温度を成長温度よりも200℃上昇させた状態で1時間保持した後に結晶成長温度まで温度を降下させた。その後、図1に例示した種結晶保持軸と同様な構造によって保持されたSiC種結晶を溶液に浸漬し、3時間の浸漬時間が経過した後、種結晶保持軸を上昇させ、種結晶を溶液から引き揚げた。実施例1で実施した溶液の高温処理および結晶成長時の溶液温度の時間変化を図2に示した。なお、結晶成長中は種結晶保持軸と黒鉛坩堝を互いに逆方向に回転させた。
Example 1
In the experiment, the graphite crucible was filled with Si, the graphite crucible and the Si raw material were kept at a temperature of about 1100 ° C. under a reduced pressure of 1 Pa or less, the adsorbed gas was degassed, and Ar gas was 0.95 MPa as the atmospheric gas. Filled to a pressure and heated so that the bottom surface of the graphite crucible was 1900 ° C. to melt the Si raw material. Thereafter, the temperature of the solution was maintained for 1 hour in a state of 200 ° C. higher than the growth temperature, and then the temperature was lowered to the crystal growth temperature. Thereafter, the SiC seed crystal held by the same structure as the seed crystal holding shaft illustrated in FIG. 1 is immersed in the solution, and after the immersion time of 3 hours has elapsed, the seed crystal holding shaft is raised, Pulled from. The time change of the solution temperature during the high temperature treatment and crystal growth of the solution carried out in Example 1 is shown in FIG. During crystal growth, the seed crystal holding shaft and the graphite crucible were rotated in opposite directions.

(比較例1)
黒鉛坩堝にSiを充填し、1Pa以下の減圧下で黒鉛坩堝及びSi原料を1100℃程度の温度に保持し、吸着ガスを脱気した後、雰囲気ガスとしてArガスを0.95MPaの圧力になるように充填し、黒鉛坩堝の底面が1900℃になるように加熱し、Si原料を融解させた。その後、図1に例示した種結晶保持軸と同様な構造によって保持されたSiC種結晶を溶液に浸漬し、3時間の浸漬時間が経過した後、種結晶保持軸を上昇させ、種結晶を溶液から引き揚げた。結晶成長中は種結晶保持軸と黒鉛坩堝を互いに逆方向に回転させた。比較例1で実施した結晶成長時の溶液温度の時間変化を図3に示した。
(Comparative Example 1)
After filling the graphite crucible with Si, holding the graphite crucible and the Si raw material at a temperature of about 1100 ° C. under a reduced pressure of 1 Pa or less, degassing the adsorbed gas, and then setting the Ar gas to a pressure of 0.95 MPa as the atmospheric gas Then, the Si crucible was heated so that the bottom surface of the graphite crucible became 1900 ° C. to melt the Si raw material. Thereafter, the SiC seed crystal held by the same structure as the seed crystal holding shaft illustrated in FIG. 1 is immersed in the solution, and after the immersion time of 3 hours has elapsed, the seed crystal holding shaft is raised, Pulled from. During crystal growth, the seed crystal holding shaft and the graphite crucible were rotated in opposite directions. The time change of the solution temperature during the crystal growth performed in Comparative Example 1 is shown in FIG.

(比較例2)
黒鉛坩堝にSiを充填し、1Pa以下の減圧下で黒鉛坩堝及びSi原料を1100℃程度の温度に保持し、吸着ガスを脱気した後、雰囲気ガスとしてArガスを0.95MPaの圧力になるように充填し、黒鉛坩堝の底面が2100℃になるように加熱し、Si原料を融解させた。その後、図1に例示した種結晶保持軸と同様な構造によって保持されたSiC種結晶を溶液に浸漬し、1時間の浸漬時間が経過した後、種結晶保持軸を上昇させ、種結晶を溶液から引き揚げた。結晶成長中は種結晶保持軸と黒鉛坩堝を互いに逆方向に回転させた。比較例2で実施した結晶成長時の溶液温度の時間変化を図4に示した。
(Comparative Example 2)
After filling the graphite crucible with Si, holding the graphite crucible and the Si raw material at a temperature of about 1100 ° C. under a reduced pressure of 1 Pa or less, degassing the adsorbed gas, and then setting the Ar gas to a pressure of 0.95 MPa as the atmospheric gas And heated so that the bottom surface of the graphite crucible was 2100 ° C., and the Si raw material was melted. Thereafter, an SiC seed crystal held by the same structure as the seed crystal holding shaft illustrated in FIG. 1 is immersed in the solution, and after the immersion time of 1 hour has elapsed, the seed crystal holding shaft is raised, Pulled from. During crystal growth, the seed crystal holding shaft and the graphite crucible were rotated in opposite directions. The time change of the solution temperature during the crystal growth performed in Comparative Example 2 is shown in FIG.

実施例1の方法によって成長したSiC結晶の、成長面および成長面に垂直な断面の透過画像を示す光学顕微鏡写真を図5に示した。図5によれば、実施例1に記載した方法によるSiC単結晶成長では、ボイド発生を抑制することが可能である。この方法では、溶液の高温処理中に、溶液中の雰囲気ガス溶解量が結晶成長温度における熱力学的平衡状態での溶解量よりも低下しており、溶液の高温処理の後、結晶成長温度に溶液温度を降下しても、溶液中の雰囲気ガス溶解量が結晶成長温度における熱力学的平衡状態での溶解量よりも低下していることがボイド抑制の要因の一つであると考えられる。   The optical microscope photograph which shows the transmission image of the cross section perpendicular | vertical to a growth surface and a growth surface of the SiC crystal grown by the method of Example 1 was shown in FIG. According to FIG. 5, void generation can be suppressed in the SiC single crystal growth by the method described in the first embodiment. In this method, during the high temperature treatment of the solution, the dissolved amount of atmospheric gas in the solution is lower than the dissolved amount in the thermodynamic equilibrium state at the crystal growth temperature. Even if the solution temperature is lowered, the fact that the amount of dissolved atmospheric gas in the solution is lower than the amount dissolved in the thermodynamic equilibrium state at the crystal growth temperature is considered to be one of the factors for suppressing the void.

比較例1の方法によって成長したSiC結晶の、成長面および成長面に垂直な断面の透過画像を示す光学顕微鏡写真を図6に示した。図6によれば、結晶成長前の溶液の高温処理を実施しない場合には、SiC単結晶中のボイドを抑制することはできない。なお、図6における黒の点がボイドである。   An optical micrograph showing a transmission image of the SiC crystal grown by the method of Comparative Example 1 and a cross section perpendicular to the growth surface is shown in FIG. According to FIG. 6, when the high temperature treatment of the solution before crystal growth is not performed, voids in the SiC single crystal cannot be suppressed. Note that the black dots in FIG. 6 are voids.

実施例1と比較例1及び比較例2によって作製したSiC単結晶中のボイド密度を下記表1に示す。   The void density in the SiC single crystal produced by Example 1, Comparative Example 1 and Comparative Example 2 is shown in Table 1 below.

表1および図6から明らかなように、実施例1に記載の結晶成長条件の中の、結晶成長前の溶液の高温処理を実施しない場合には、成長させたSiC単結晶中のボイド発生を抑制することはできない。   As apparent from Table 1 and FIG. 6, in the crystal growth conditions described in Example 1, when the high-temperature treatment of the solution before crystal growth is not performed, voids are generated in the grown SiC single crystal. It cannot be suppressed.

表1から明らかなように、比較例1に記載の結晶成長条件よりも、単に成長温度を200℃上昇させた比較例2に記載の結晶成長条件を用いたSiC単結晶成長では、ボイド発生が若干低減するが、ボイド発生を大幅に抑制する効果はない。   As is apparent from Table 1, void generation is not generated in the SiC single crystal growth using the crystal growth conditions described in Comparative Example 2 in which the growth temperature is simply increased by 200 ° C. compared to the crystal growth conditions described in Comparative Example 1. Although slightly reduced, there is no effect of greatly suppressing the generation of voids.

(実施例2)
溶液原料をSi0.77Ti0.23とし、Si−C−Ti溶液に変更した以外は実施例1と同様にしてSiC単結晶を製造した。
(Example 2)
A SiC single crystal was produced in the same manner as in Example 1 except that the solution raw material was changed to Si 0.77 Ti 0.23 and changed to a Si—C—Ti solution.

(実施例3)
溶液原料をSi0.6Cr0.4とし、Si−C−Cr溶液に変更した以外は実施例1と同様にしてSiC単結晶を製造した。
(Example 3)
A SiC single crystal was produced in the same manner as in Example 1 except that the solution raw material was changed to Si 0.6 Cr 0.4 and changed to a Si—C—Cr solution.

実施例2および実施例3においても、ボイド発生を大幅に抑制することが可能であった。   Also in Example 2 and Example 3, it was possible to significantly suppress the generation of voids.

本発明のSiC単結晶の製造方法によれば、高い結晶成長温度でかつ雰囲気ガス圧力が0.1MPa以上の圧力であっても、ボイドの発生を大幅に抑制し、ボイドを含まない高品質のSiC単結晶を製造することが可能となる。   According to the method for producing a SiC single crystal of the present invention, even when the crystal growth temperature is high and the atmospheric gas pressure is 0.1 MPa or more, the generation of voids is greatly suppressed, and high quality without containing voids. It becomes possible to produce a SiC single crystal.

1 黒鉛坩堝
2 SiC種結晶
3 種結晶保持軸
4 溶液
5 断熱材
6 高周波コイル
1 graphite crucible 2 SiC seed crystal 3 seed crystal holding shaft 4 solution 5 heat insulating material 6 high frequency coil

Claims (7)

Si及びCを含む溶液中に、SiCの種結晶を浸漬し、溶液成長法によりSiCを析出・成長させるにあたり、該種結晶を該溶液に浸漬する前に、該溶液の温度を一時的に結晶成長温度よりも50〜300℃高温に保って製造して、結晶成長部分のボイド密度を10000個/cm以下としたことを特徴とするSiC単結晶。 In immersing SiC seed crystals in a solution containing Si and C, and precipitating and growing SiC by the solution growth method, the temperature of the solution is temporarily crystallized before immersing the seed crystals in the solution. A SiC single crystal produced by maintaining a temperature higher by 50 to 300 ° C. than the growth temperature, and having a void density in the crystal growth portion of 10,000 pieces / cm 3 or less. Si及びCを含む溶液中に、SiCの種結晶を浸漬し、SiCを析出・成長させる溶液成長法によるSiC単結晶の製造方法であって、該種結晶を該溶液に浸漬する前に、該溶液の温度を一時的に結晶成長温度よりも50〜300℃高温に保つことを特徴とするSiC単結晶の製造方法。   A method for producing a SiC single crystal by a solution growth method in which a SiC seed crystal is immersed in a solution containing Si and C, and SiC is precipitated and grown, and before the seed crystal is immersed in the solution, A method for producing a SiC single crystal, characterized in that the temperature of the solution is temporarily maintained at a temperature higher by 50 to 300 ° C than the crystal growth temperature. 前記溶液の温度を一時的に前記結晶成長温度よりも高温に保つ時間が10分以上、3時間以下であることを特徴とする請求項2に記載のSiC単結晶の製造方法。   3. The method for producing an SiC single crystal according to claim 2, wherein the time during which the temperature of the solution is temporarily kept higher than the crystal growth temperature is 10 minutes or longer and 3 hours or shorter. 前記SiC単結晶の製造をガス雰囲気下で行い、該雰囲気ガスの圧力が0.1MPa以上の加圧条件に設定されていることを特徴とする請求項2または3に記載のSiC単結晶の製造方法。   The production of the SiC single crystal according to claim 2 or 3, wherein the production of the SiC single crystal is performed in a gas atmosphere, and the pressure of the atmospheric gas is set to a pressure condition of 0.1 MPa or more. Method. 前記結晶成長温度が、1700〜2100℃の範囲内であることを特徴とする請求項2〜4のいずれか1項に記載のSiC単結晶の製造方法。   The said crystal growth temperature exists in the range of 1700-2100 degreeC, The manufacturing method of the SiC single crystal of any one of Claims 2-4 characterized by the above-mentioned. 前記溶液中に遷移金属元素および/または希土類元素を含むことを特徴とする請求項2〜5のいずれかに記載のSiC単結晶の製造方法。   The method for producing a SiC single crystal according to any one of claims 2 to 5, wherein the solution contains a transition metal element and / or a rare earth element. 請求項2〜6のいずれか1項に記載の製造方法で製造されたSiC単結晶。   The SiC single crystal manufactured with the manufacturing method of any one of Claims 2-6.
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