JP2012162439A - METHOD FOR MANUFACTURING SiC SINGLE CRYSTAL BY SOLUTION METHOD - Google Patents
METHOD FOR MANUFACTURING SiC SINGLE CRYSTAL BY SOLUTION METHOD Download PDFInfo
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Abstract
【課題】成長結晶端部のクラック発生を防止して、溶液法によりSiC単結晶を製造する方法を提供する。
【解決手段】Si−C溶液面に接触させたSiC種結晶の下面にSiC単結晶を成長させる、溶液法によるSiC単結晶の製造方法において、結晶成長が完了した時に、成長したSiC単結晶が接触している上記溶液面の近傍のSi−C溶液のC濃度を低下させた後に、上記成長したSiC単結晶を上記溶液面から引き上げることを特徴とする溶液法によるSiC単結晶の製造方法。成長したSiC単結晶が接触している上記溶液面の近傍のSi−C溶液のC濃度を7at%以下に低下させることが望ましい。
【選択図】図2The present invention provides a method for producing a SiC single crystal by a solution method by preventing the occurrence of cracks at the edge of a grown crystal.
In a method for producing an SiC single crystal by a solution method in which an SiC single crystal is grown on the lower surface of an SiC seed crystal brought into contact with the Si-C solution surface, the grown SiC single crystal is formed when the crystal growth is completed. A method for producing an SiC single crystal by a solution method, wherein the grown SiC single crystal is pulled up from the solution surface after the C concentration of the Si-C solution in the vicinity of the solution surface in contact is lowered. It is desirable to reduce the C concentration of the Si—C solution in the vicinity of the solution surface in contact with the grown SiC single crystal to 7 at% or less.
[Selection] Figure 2
Description
本発明は、溶液法によるSiC単結晶の製造方法に関し、特に成長結晶端部のクラック防止に関する。 The present invention relates to a method for producing a SiC single crystal by a solution method, and particularly to prevention of cracks at the edge of a grown crystal.
溶液法によるSiC単結晶の製造方法は、Si−C溶液面に接触させたSiC種結晶の下面にSiC単結晶を成長させる方法である。結晶成長完了時に成長結晶を引き上げて端部を溶液面から離す際に、成長端部にSi−C溶液が付着する。付着溶液が固化する際の応力により、端部にクラックが発生するという問題があった。 The manufacturing method of the SiC single crystal by the solution method is a method of growing the SiC single crystal on the lower surface of the SiC seed crystal brought into contact with the Si—C solution surface. When the growth crystal is pulled up and the end portion is separated from the solution surface when the crystal growth is completed, the Si—C solution adheres to the growth end portion. There was a problem that cracks occurred at the end due to the stress when the adhesion solution solidified.
Si単結晶の溶液法による製造方法では、同様に溶液の付着があっても、固化時に膨張するため圧縮応力が作用するため、SiC単結晶におけるようなクラック発生の問題は生じない。また、成長端部の径を制御して凸状にすることで、クラック発生の危険性がある端部は用いないという方法もあるが、歩留まりが低下するという問題がある。特に、成長速度が遅いSiC単結晶の場合は無視できない歩留まり低下が避けられない。 In the production method of the Si single crystal by the solution method, even if the solution adheres, the problem of crack generation as in the SiC single crystal does not occur because the compressive stress acts because it expands at the time of solidification. In addition, there is a method of controlling the diameter of the growth end portion so as to make it convex so that the end portion having a risk of occurrence of cracks is not used, but there is a problem that the yield decreases. In particular, in the case of a SiC single crystal having a slow growth rate, a yield reduction that cannot be ignored is inevitable.
その対策として、特許文献1には、成長結晶を引き上げる際に、成長結晶を高速回転させて付着溶液を飛散させることが提案されている。しかしこの方法では、遠心力がかからないため結晶中央部の付着溶液を完全に除去することが困難であり、端部に付着溶液が残留して多結晶化し、クラックの原因になるという問題があった。 As a countermeasure, Patent Document 1 proposes that when the growth crystal is pulled up, the growth solution is rotated at a high speed to disperse the adhesion solution. However, with this method, it is difficult to completely remove the adhesion solution at the center of the crystal because no centrifugal force is applied, and there is a problem that the adhesion solution remains at the end portion to be polycrystallized and cause cracks. .
また、特許文献2には、結晶成長に用いるSi−C溶液の容器を収容した炉の内部に、Cを含有しないSi融液の容器を更に収容し、SiC単結晶をSi−C溶液から引き上げた後に、Si融液に浸して付着溶液を洗い流すことが提案されている。しかしこの方法では、成長用容器の他に洗い流すための容器を収容するには、炉を含めた結晶成長装置の容量をかなり大きくして炉のホットゾーンを拡大する必要がある。更に、SiC単結晶の成長のように高温を必要とする場合、結晶成長に必要な温度分布を形成することが困難になるという問題があった。 In Patent Document 2, a Si melt container not containing C is further housed in a furnace containing a Si—C solution container used for crystal growth, and the SiC single crystal is pulled up from the Si—C solution. After that, it has been proposed to wash away the adhering solution by immersing in Si melt. However, in this method, it is necessary to expand the hot zone of the furnace by considerably increasing the capacity of the crystal growth apparatus including the furnace in order to accommodate the container for washing out in addition to the growth container. Furthermore, when a high temperature is required as in the growth of a SiC single crystal, there is a problem that it is difficult to form a temperature distribution necessary for crystal growth.
本発明は、上記従来技術の欠点を解消し、成長結晶端部のクラック発生を防止して、溶液法によりSiC単結晶を製造する方法を提供することを目的とする。 An object of the present invention is to provide a method for producing a SiC single crystal by a solution method by solving the above-described drawbacks of the prior art, preventing cracks from occurring at the edge of the grown crystal.
上記の目的を達成するために、本発明によれば、Si−C溶液面に接触させたSiC種結晶の下面にSiC単結晶を成長させる、溶液法によるSiC単結晶の製造方法において、結晶成長が完了した時に、成長したSiC単結晶が接触している上記溶液面の近傍のSi−C溶液のC濃度を低下させた後に、上記成長したSiC単結晶を上記溶液面から引き上げることを特徴とする溶液法によるSiC単結晶の製造方法が提供される。 In order to achieve the above object, according to the present invention, in the method for producing an SiC single crystal by a solution method, an SiC single crystal is grown on the lower surface of an SiC seed crystal in contact with the Si-C solution surface. When the step is completed, the grown SiC single crystal is pulled up from the solution surface after the C concentration of the Si-C solution in the vicinity of the solution surface in contact with the grown SiC single crystal is lowered. A method for producing a SiC single crystal by a solution method is provided.
本発明によれば、成長結晶端部に付着するSi−C溶液のC濃度が低下しているので、固化時に発生する応力が軽減され、クラックの発生が防止される。 According to the present invention, since the C concentration of the Si—C solution adhering to the grown crystal edge is reduced, the stress generated during solidification is reduced, and the generation of cracks is prevented.
溶液法によるSiC単結晶の成長法においては、溶液のC濃度が低いとSiC単結晶の成長速度が遅い(最大で70μm/hr程度)ため、溶液のC溶解度を高める第3元素(Cr等)を添加してC濃度を高めることが一般的である。しかし、C濃度が高いと付着溶液の固化時に成長結晶と結合してクラックが発生する。本発明においては、結晶成長中は成長速度を確保するために必要なC濃度を維持し、結晶成長完了時にC濃度を低下させてクラックの発生を防止する。 In the growth method of the SiC single crystal by the solution method, when the C concentration of the solution is low, the growth rate of the SiC single crystal is slow (about 70 μm / hr at the maximum), so the third element (Cr or the like) that increases the C solubility of the solution It is common to increase the C concentration by adding. However, if the C concentration is high, cracks occur due to bonding with the grown crystals when the adhesion solution is solidified. In the present invention, the C concentration necessary for securing the growth rate is maintained during the crystal growth, and the C concentration is lowered when the crystal growth is completed to prevent the generation of cracks.
結晶成長完了時にC濃度を低下させる方法は、下記のいずれかによる。 The method for reducing the C concentration upon completion of crystal growth is as follows.
(1)成長結晶を引き上げる直前に、Si−C溶液の温度を低下させる。 (1) The temperature of the Si—C solution is lowered immediately before pulling up the grown crystal.
(2)成長結晶を引き上げる直前に、Si−C溶液のC溶解度を上げない元素を添加する。 (2) An element that does not increase the C solubility of the Si—C solution is added immediately before pulling up the grown crystal.
(3)成長結晶をSi−C溶液が固化しない温度まで昇温させ、Si−C溶液のC溶解度を上げない元素を添加してから、成長結晶を引き上げる。 (3) The growth crystal is heated to a temperature at which the Si—C solution does not solidify, an element that does not increase the C solubility of the Si—C solution is added, and then the growth crystal is pulled up.
上記(1)のSi−C溶液の温度を下げる方法としては下記のいずれかが可能である。 As the method for lowering the temperature of the Si-C solution (1), any of the following methods is possible.
(a)高周波コイルの出力を下げる
(b)高周波コイルに対する坩堝位置を変更する
上記(2)(3)で用いる、Si−C溶液のC溶解度を上げない元素としてはSiが最も適している。しかしSiに限定する必要はなく、Co,Nd,Py等の希土類元素、Al,Ga,In,Ti,P,As,Sb,Bi,Mo,Ni、等を用いることもできる。
(A) Decreasing the output of the high-frequency coil (b) Changing the crucible position with respect to the high-frequency coil Si is most suitable as an element used in the above (2) and (3) that does not increase the C solubility of the Si—C solution. However, it is not necessary to limit to Si, and rare earth elements such as Co, Nd, and Py, Al, Ga, In, Ti, P, As, Sb, Bi, Mo, Ni, and the like can also be used.
なお、成長結晶を引き上げる際には、成長結晶端部への溶液の付着を低減させるために、成長結晶を回転させることが望ましい。 When pulling up the growth crystal, it is desirable to rotate the growth crystal in order to reduce the adhesion of the solution to the edge of the growth crystal.
また、添加元素の供給は、黒鉛製の筒を介して粒状の元素(Si等)を溶液中に投入することができる。添加元素提供時には、溶液の回転等の溶質の攪拌を促進する工程を停止する事で、溶液を流動させない事が望ましい。また、溶液のC濃度を下げる時は、単結晶が接触している溶液近傍のC濃度を下げる事で、溶液におけるC濃度を下げる対象とする領域を絞り込むことができる。更にそのC濃度を下げる対象とする領域は成長した単結晶を引き上げる工程で単結晶に付着しうる領域である事が望ましい。そうすることによって、結晶引き上げ時に付着する溶液のC濃度をより確実に減らす事ができる。また、C濃度を減少させる操作後は、C濃度が減少した領域が拡散しないように、溶液の攪拌を行わない事が望ましい。 The additive element can be supplied by introducing a granular element (Si or the like) into the solution via a graphite tube. When providing the additive element, it is desirable not to cause the solution to flow by stopping the step of promoting the stirring of the solute such as the rotation of the solution. Moreover, when lowering the C concentration of the solution, by reducing the C concentration in the vicinity of the solution in contact with the single crystal, it is possible to narrow the target region for lowering the C concentration in the solution. Further, it is desirable that the region to be reduced in C concentration is a region that can adhere to the single crystal in the step of pulling up the grown single crystal. By doing so, the C concentration of the solution adhering at the time of crystal pulling can be more reliably reduced. Further, after the operation of reducing the C concentration, it is desirable not to stir the solution so that the region where the C concentration is reduced does not diffuse.
図1に示した結晶成長装置により、表1に示したようにSi−C溶液のC濃度を2at%〜17at%に変化させ、種結晶4H−SiCを用いて、成長温度1900℃でSiC単結晶を成長させた。 The crystal growth apparatus shown in FIG. 1 is used to change the C concentration of the Si—C solution from 2 at% to 17 at% as shown in Table 1, and using a seed crystal 4H—SiC at a growth temperature of 1900 ° C. at a single crystal of SiC. Crystals were grown.
成長結晶の端部におけるクラック発生の有無を調べ、表1に併せて示した。なお、表1中で、○はクラック発生なし、×はクラック発生ありを示す。0/5などの分数(n1/n2)は、分子(n1)がクラック発生サンプル数、分母(n2)が全サンプル数を示す。 The presence or absence of cracks at the end of the grown crystal was examined and is shown in Table 1. In Table 1, ◯ indicates that no crack is generated, and × indicates that a crack is generated. For fractions (n1 / n2) such as 0/5, the numerator (n1) indicates the number of cracked samples, and the denominator (n2) indicates the total number of samples.
図2に、Si−C溶液のC濃度を17at%とした場合の成長結晶端部の(1A)成長したまま(as-grown)および(1B)酸処理後の状態、およびSi−C溶液のC濃度を2at%とした場合の成長結晶端部の(2A)成長したまま(as-grown)および(2B)酸処理後の状態を、それぞれ写真で示す。 FIG. 2 shows (1A) the as-grown and (1B) state after the acid treatment at the edge of the grown crystal when the C concentration of the Si—C solution is 17 at%, and the Si—C solution. When the C concentration is 2 at%, (2A) the as-grown state and (2B) the state after the acid treatment at the edge of the grown crystal are shown by photographs.
C濃度17at%の場合は酸処理によりクラック発生部位から剥離が生じている。これに対してC濃度2at%の場合は酸処理による剥離が全く生じていない。このように、酸処理によって、クラック発生の有無を明瞭に判定できた。 In the case where the C concentration is 17 at%, peeling occurs from the crack generation site due to the acid treatment. On the other hand, when the C concentration is 2 at%, peeling due to acid treatment does not occur at all. Thus, the presence or absence of crack generation could be clearly determined by the acid treatment.
この結果から、C濃度を7at%以下にすることにより、成長結晶端部のクラック発生を完全に防止できることが分かる。 From this result, it can be seen that by making the C concentration 7 at% or less, the generation of cracks at the edge of the grown crystal can be completely prevented.
本実施例では、本発明の方法のシミュレーションとして、初めからC濃度を種々に変えたSi−C溶液を用いてSiC単結晶成長を行なったが、結晶成長完了後にC濃度を変えた(低下させた)場合も、同等の効果が得られると考えられる。 In this example, as a simulation of the method of the present invention, SiC single crystal growth was performed using a Si—C solution in which the C concentration was changed from the beginning. However, the C concentration was changed (lowered) after the completion of crystal growth. In this case, the same effect can be obtained.
本発明に従ってSi−C溶液のC溶解度を上げない元素を添加する場合は、図1に仮想線で示したように、黒鉛製等の原料供給筒を介して添加するとよい。この場合、筒の先端はSi−C溶液に接触させないようにして、余分なCの添加を防止する。 When adding an element that does not increase the C solubility of the Si—C solution in accordance with the present invention, it may be added via a raw material supply cylinder such as graphite as shown by the phantom line in FIG. In this case, the tip of the cylinder is not brought into contact with the Si—C solution to prevent the addition of excess C.
本発明によれば、上記従来技術の欠点を解消し、成長結晶端部のクラック発生を防止して、溶液法によりSiC単結晶を製造する方法が提供される。すなわち、成長結晶端部に付着するSi−C溶液のC濃度が低下しているので、固化時に発生する応力が軽減され、クラックの発生が防止される。 According to the present invention, there is provided a method for producing a SiC single crystal by a solution method, which eliminates the above-mentioned drawbacks of the prior art, prevents the occurrence of cracks at the edge of the grown crystal. That is, since the C concentration of the Si—C solution adhering to the edge of the grown crystal is reduced, the stress generated during solidification is reduced and the generation of cracks is prevented.
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| JP2015101532A (en) * | 2013-11-28 | 2015-06-04 | 京セラ株式会社 | Method of manufacturing crystal |
| WO2015115543A1 (en) * | 2014-01-29 | 2015-08-06 | 京セラ株式会社 | Method for manufacturing crystal |
| JP2017061391A (en) * | 2015-09-24 | 2017-03-30 | トヨタ自動車株式会社 | Method for producing SiC single crystal |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP2015101532A (en) * | 2013-11-28 | 2015-06-04 | 京セラ株式会社 | Method of manufacturing crystal |
| WO2015115543A1 (en) * | 2014-01-29 | 2015-08-06 | 京セラ株式会社 | Method for manufacturing crystal |
| JP2016179942A (en) * | 2014-01-29 | 2016-10-13 | 京セラ株式会社 | Crystal production process |
| JP6014258B2 (en) * | 2014-01-29 | 2016-10-25 | 京セラ株式会社 | Crystal production method |
| JP2017024985A (en) * | 2014-01-29 | 2017-02-02 | 京セラ株式会社 | Crystal production method |
| US10443149B2 (en) | 2014-01-29 | 2019-10-15 | Kyocera Corporation | Method of producing crystal |
| JP2017061391A (en) * | 2015-09-24 | 2017-03-30 | トヨタ自動車株式会社 | Method for producing SiC single crystal |
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