JPH0940486A - Single crystal manufacturing method - Google Patents
Single crystal manufacturing methodInfo
- Publication number
- JPH0940486A JPH0940486A JP19336495A JP19336495A JPH0940486A JP H0940486 A JPH0940486 A JP H0940486A JP 19336495 A JP19336495 A JP 19336495A JP 19336495 A JP19336495 A JP 19336495A JP H0940486 A JPH0940486 A JP H0940486A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- material rod
- single crystal
- seed crystal
- oxygen concentration
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C30—CRYSTAL GROWTH
- C30B—SINGLE-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
- C30B13/00—Single-crystal growth by zone-melting; Refining by zone-melting
- C30B13/16—Heating of the molten zone
- C30B13/22—Heating of the molten zone by irradiation or electric discharge
- C30B13/24—Heating of the molten zone by irradiation or electric discharge using electromagnetic waves
Landscapes
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Engineering & Computer Science (AREA)
- Crystallography & Structural Chemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
Abstract
(57)【要約】
【課題】 フローティングゾーン法における単結晶の大
径化を可能とし、原料棒と種結晶の接合を容易とする。
【解決手段】 フローティングゾーン法により単結晶を
製造する際に、原料棒と種結晶の接合後、単結晶育成方
向において次第に大径とされ、種結晶よりも大径とされ
る肩部を形成し、この上に円筒状の直胴部を形成する。
なお、接合後から肩部形成までの雰囲気ガス中の酸素濃
度Co1 、肩部形成時の酸素濃度Co2 、直胴部形成時
の酸素濃度Co3 がCo1 =Co3 、Co1 <Co2 、
Co3 <Co2 の関係を有することが好ましい。また、
上記のようにして単結晶を製造するに際し、原料棒及び
種結晶を融点近傍における液体の密度が固体の密度より
も小さい材料系により形成し、原料棒と種結晶の接合時
の雰囲気ガス中の酸素濃度を後工程における酸素濃度よ
りも低くする。(57) 【Abstract】 PROBLEM TO BE SOLVED: To increase the diameter of a single crystal in a floating zone method, and to easily bond a raw material rod and a seed crystal. When manufacturing a single crystal by a floating zone method, after joining a raw material rod and a seed crystal, a shoulder portion having a larger diameter in the single crystal growth direction and a larger diameter than the seed crystal is formed. A cylindrical straight body portion is formed on this.
It should be noted that the oxygen concentration Co 1 in the atmospheric gas from the joining to the shoulder formation, the oxygen concentration Co 2 during the shoulder formation, and the oxygen concentration Co 3 during the straight body formation are Co 1 = Co 3 and Co 1 <Co 2 ,
It is preferable to have a relationship of Co 3 <Co 2 . Also,
When manufacturing a single crystal as described above, the material rod and the seed crystal are formed by a material system in which the density of the liquid in the vicinity of the melting point is lower than the density of the solid, and the material rod and the seed crystal are mixed in the atmosphere gas at the time of bonding. The oxygen concentration is made lower than the oxygen concentration in the subsequent process.
Description
【0001】[0001]
【発明の属する技術分野】本発明は電子材料等に使用さ
れる単結晶の製造方法に関する。詳しくはフローティン
グゾーン法を適用した単結晶の製造方法において、チョ
コラルスキー法において一般的である肩部を形成し、大
径の単結晶を製造することを可能とする単結晶の製造方
法及び原料棒と種結晶の接合時の酸素濃度を低くし、こ
れらの接合を容易とする単結晶の製造方法に係るもので
ある。TECHNICAL FIELD The present invention relates to a method for producing a single crystal used for electronic materials and the like. Specifically, in the method for producing a single crystal to which the floating zone method is applied, a shoulder which is common in the Czochralski method, and a method for producing a single crystal capable of producing a large diameter single crystal and a raw material rod The present invention relates to a method for producing a single crystal in which the oxygen concentration at the time of joining a seed crystal and a seed crystal is lowered to facilitate the joining.
【0002】[0002]
【従来の技術】シリコン,水晶,ダイヤモンド,サファ
イヤ等の単結晶材料は電子材料やその他の材料として多
用されており、その製造技術は各種産業分野において重
要なものとなっている。2. Description of the Related Art Single crystal materials such as silicon, quartz, diamond and sapphire are widely used as electronic materials and other materials, and their manufacturing techniques are important in various industrial fields.
【0003】単結晶の製造方法としては、融液法,溶液
法,固相法,気相法が挙げられるが、例えば融液法を適
用した単結晶の製造方法としては主にチョコラルスキー
法(以下、Cz法と称する。)、フローティングゾーン
法(以下、Fz法と称する。)が挙げられる。Examples of the method for producing a single crystal include a melt method, a solution method, a solid phase method, and a gas phase method. For example, a method for producing a single crystal to which the melt method is applied is mainly the Czochralski method ( Hereinafter, the Cz method will be referred to) and the floating zone method (hereinafter referred to as the Fz method) will be mentioned.
【0004】上記Cz法は、るつぼ内の融液に種結晶を
接触させ、種結晶或いは種結晶とるつぼの両方を回転さ
せながら単結晶を引き上げる方法である。上記Cz法は
メルトと単結晶が融けた場合の組成が同一である一致溶
融化合物を対象にした材料の単結晶の製造に使用されて
いる。また、上記Cz法は、製造装置の制御が容易であ
り、大径の単結晶の製造が可能であることから、量産性
が良好である。The Cz method is a method in which a seed crystal is brought into contact with the melt in the crucible and the single crystal is pulled while rotating both the seed crystal and the crucible for taking the seed crystal. The Cz method is used for producing a single crystal of a material intended for a congruent melting compound having the same composition when the melt and the single crystal are melted. In addition, the Cz method is easy to control the manufacturing apparatus and is capable of manufacturing a large-diameter single crystal, and thus has good mass productivity.
【0005】なお、上記Cz法においては、単結晶中へ
の欠陥の混入を防ぐために、種結晶を融液に接触させた
後、比較的小径のネッキング部と称される部分を製造
し、単結晶育成方向において次第に大径とされ、種結晶
よりも大径とされる肩部と称される部分を形成し、続い
て円筒状の直胴部と称される部分を形成するようにして
単結晶を製造している。In the above Cz method, in order to prevent the inclusion of defects into the single crystal, a seed crystal is brought into contact with the melt, and then a portion called a necking portion having a relatively small diameter is manufactured. The diameter is gradually increased in the crystal growth direction to form a portion called a shoulder portion having a diameter larger than that of the seed crystal, and then a portion called a cylindrical straight body portion is formed. Manufacturing crystals.
【0006】しかしながら、上記Cz法においてはるつ
ぼを使用するため、るつぼ材の融点、材料の融点、双方
の反応性を考慮する必要があり、使用可能な材料が限定
されるという欠点がある。また、上記Cz法は、一方向
の凝固法であるため、組成ずれが生じない系で上述のよ
うにメルトと結晶が融けた場合の組成が同一である一致
溶融化合物の材料の単結晶の製造にしか適用できず、こ
のことからも使用可能な材料が限定される。さらに、上
記Cz法においては、メルトの蒸散による組成ずれを避
けるために低蒸気圧の材料の単結晶の製造にしか適用で
きず、このことからも使用可能な材料が限定される。However, since the crucible is used in the Cz method, it is necessary to consider the melting point of the crucible material, the melting point of the material, and the reactivity of both, and there is a drawback that usable materials are limited. In addition, since the Cz method is a unidirectional solidification method, a single crystal of a material of a congruent melting compound having the same composition when the melt and the crystal are melted as described above in a system in which composition deviation does not occur It is only applicable to the above, and this also limits the usable materials. Further, the above Cz method can be applied only to the production of a single crystal of a low vapor pressure material in order to avoid composition shift due to evaporation of the melt, and this also limits the usable materials.
【0007】一方、上記Fz法は原料棒を両端で鉛直に
保持し、その一部を加熱溶融して溶融帯を形成し、これ
を一端側から他端側へと移動して順次単結晶化する方法
である。上記Fz法は、主に高融点材料或いは分解溶融
化合物の結晶の製造に使用されている。On the other hand, in the above Fz method, the raw material rod is held vertically at both ends, and a part of it is heated and melted to form a molten zone, which is moved from one end side to the other end side to successively form a single crystal. Is the way to do it. The Fz method is mainly used for producing crystals of high melting point materials or decomposed and fused compounds.
【0008】上記Fz法は、るつぼを使用しないため、
るつぼ材による汚染がなく、加熱するヒーター材が限定
されないことから、育成可能な温度領域を広くすること
が可能である。また、上記Fz法においては、原料棒同
士からでも単結晶の製造が可能である上、少量の原料粉
からでも単結晶の製造が可能であることから材料探査等
に適している。さらに、上記Fz法においては、一致溶
融化合物だけでなく分解溶融化合物の単結晶の製造も可
能であり、使用可能な材料が比較的限定されない。さら
にまた、上記Fz法を適用した製造装置は閉じた装置系
となり、単結晶の製造を閉じた系の中で行うこととなる
ため、雰囲気の制御が容易である。Since the Fz method does not use a crucible,
Since there is no contamination by the crucible material and the heater material to be heated is not limited, it is possible to widen the temperature range in which growth is possible. Further, the Fz method is suitable for material exploration and the like because it is possible to manufacture single crystals from raw material rods, and also to manufacture single crystals from a small amount of raw material powder. Furthermore, in the above Fz method, not only the congruent melting compound but also a single crystal of a decomposition melting compound can be produced, and the usable material is relatively limited. Furthermore, since the manufacturing apparatus to which the above Fz method is applied is a closed apparatus system and the single crystal is manufactured in the closed system, the atmosphere can be easily controlled.
【0009】しかしながら、上記Fz法においては、大
径の単結晶の製造が困難であり、単結晶の大型化に対応
が困難であるといった不都合を有している。However, the Fz method has a disadvantage that it is difficult to manufacture a large-diameter single crystal and it is difficult to cope with an increase in size of the single crystal.
【0010】[0010]
【発明が解決しようとする課題】上述のようにFz法に
おいて大型の単結晶の製造が困難であるのは、以下のよ
うな理由による。The reason why it is difficult to produce a large single crystal by the Fz method as described above is as follows.
【0011】上記Fz法は、溶融帯を原料棒内で相対的
に移動させて順次単結晶化するものであるため、原料棒
から送り込んだ分だけ単結晶が晶出され単結晶が育成さ
れる。従って、単結晶を大径化するには、原料棒の送り
込み速度を単結晶の育成速度よりも相対的に速くする方
法が用いられる。In the above Fz method, the melting zone is relatively moved within the raw material rod to sequentially form a single crystal. Therefore, the single crystal is crystallized by the amount fed from the raw material rod to grow the single crystal. . Therefore, in order to increase the diameter of the single crystal, a method of making the feed rate of the raw material rod relatively faster than the growth rate of the single crystal is used.
【0012】ところで、上記Fz法においては、溶融帯
は溶融帯自体の表面張力と重力のバランスにより保持さ
れており、表面張力が小さく、密度も大きい材料系にお
いては溶融帯を保持することが難しい。By the way, in the above Fz method, the melting zone is held by the balance between the surface tension and gravity of the melting zone itself, and it is difficult to hold the melting zone in a material system having a small surface tension and a high density. .
【0013】従って、このような材料系を使用した場合
において、上記のような方法で単結晶の大径化を行おう
とすると、溶融帯を保持することが困難で、溶融帯の垂
れが生じ、単結晶の大径化は困難である。Therefore, when such a material system is used, if the diameter of the single crystal is increased by the method as described above, it is difficult to hold the melting zone and the melting zone sags. It is difficult to increase the diameter of a single crystal.
【0014】また、上記Fz法においては、種結晶上に
単結晶を育成するのが一般的であり、種結晶と原料棒を
溶融部を介して接合し、上記溶融部を最初の溶融帯とし
て上記のような方法で単結晶の製造を行う。このとき、
前述のように上記種結晶及び原料棒が高融点材料である
ことから、加熱手段として使用される例えば赤外線ラン
プとしては高出力のものを使用することが望ましい。Further, in the above Fz method, it is general to grow a single crystal on a seed crystal, and the seed crystal and the raw material rod are joined together through a fusion zone, and the fusion zone is used as the first fusion zone. A single crystal is manufactured by the method as described above. At this time,
Since the seed crystal and the raw material rod are high melting point materials as described above, it is desirable to use, for example, an infrared lamp having a high output as the heating means.
【0015】ところが、上記赤外線ランプとしては、通
常、ランニングコストの安価なハロゲンランプが使用さ
れており、大出力のハロゲンランプにおいてはランプの
フィラメントが大きくなる傾向があり、その分、集光が
ブロードになり、集光部の加熱により形成される溶融帯
が大きくなってしまう。すなわち、溶融帯の垂れが発生
する可能性も高くなり、単結晶の大径化が困難となって
しまう。However, as the infrared lamp, a halogen lamp having a low running cost is usually used, and in a halogen lamp having a large output, the filament of the lamp tends to be large. As a result, the melting zone formed by heating the condensing part becomes large. That is, there is a high possibility that the melted zone will sag, and it will be difficult to increase the diameter of the single crystal.
【0016】従って、上述のように単結晶の大径化を行
うためには、ランプとしてできるだけ小出力のものを使
用し、集光度を高めることが好ましく、上記のような種
結晶と原料棒の溶融部を介した接合は困難である。Therefore, in order to increase the diameter of the single crystal as described above, it is preferable to use a lamp having a small output as much as possible to enhance the light converging power. Joining via the fusion zone is difficult.
【0017】そこで、本発明は従来の実情に鑑みて提案
されたものであり、Fz法における単結晶の大径化を可
能とする単結晶の製造方法及び原料棒と種結晶の接合を
容易とする単結晶の製造方法を提供することを目的とす
る。Therefore, the present invention has been proposed in view of the conventional circumstances, and facilitates the manufacturing method of a single crystal and the joining of a raw material rod and a seed crystal, which can increase the diameter of the single crystal in the Fz method. It is an object of the present invention to provide a method for producing a single crystal that
【0018】[0018]
【課題を解決するための手段】上述の目的を達成するた
めに本発明者等が鋭意検討した結果、Fz法においても
Cz法において単結晶への欠陥の混入を防止するべく実
施されている肩部及び直胴部の形成を行えば、最終的に
は種結晶よりも大径となる肩部の上にそのままの径を有
する直胴部が形成されることから、単結晶の大径化が可
能であることを見い出した。そして、このようにして単
結晶を製造すれば、Fz法の利点を生かした良質な単結
晶が製造される。Means for Solving the Problems As a result of intensive studies made by the present inventors in order to achieve the above-mentioned object, the Fz method and the Cz method have been carried out to prevent the inclusion of defects into a single crystal. If the diameter of the single crystal is increased, the diameter of the single crystal is increased because the diameter of the single body is formed on the shoulder that has a diameter larger than that of the seed crystal. I found it possible. When a single crystal is manufactured in this manner, a good quality single crystal that makes the most of the advantages of the Fz method is manufactured.
【0019】一般に、Cz法及びTSSG(Top−S
eeded Solution Growth)法等に
おける融液成長及び溶液成長の酸化物の単結晶育成で
は、固体を融かして(溶かして)から種結晶を用いて融
液(溶液)の温度を下げながら単結晶を晶出させて単結
晶を育成している。In general, the Cz method and TSSG (Top-S
In the single crystal growth of the melt-grown and solution-grown oxides in the seeded solution growth method, etc., the single crystal is melted (melted) and then the seed crystal is used to lower the temperature of the melt (solution). Are crystallized to grow a single crystal.
【0020】近年、上記のような融液成長の分野で、例
えば木村茂行により、融液成長による単結晶育成におい
て融液の物性が単結晶育成の制御の重要な因子となって
いることが指摘されている。(結晶成長国内会議 特別
講演 1992年 7月) すなわち、融液の結晶成長においては、融液の粘性及び
表面張力を下げることが、融液を均一に攪拌できること
につながり、液体である融液から固体である結晶に均一
に物質を供給することを可能とするので望ましいとされ
ている。In recent years, in the field of melt growth as described above, for example, Shigeyuki Kimura pointed out that the physical properties of the melt have become important factors for controlling the growth of the single crystal in the growth of the single crystal by the melt growth. Has been done. (National Conference on Crystal Growth, Special Lecture, July 1992) That is, in crystal growth of a melt, lowering the viscosity and surface tension of the melt leads to uniform agitation of the melt, and the melt from a liquid is melted. It is desirable because it allows a substance to be uniformly supplied to a solid crystal.
【0021】そして、例えば酸化物の融液では原子が規
則正しく並んで結合した固体とは異なり、原子はより自
由度をもっていると考えられるが、液体表面では酸素原
子を介して他の原子と架橋(ダングルボンド)を形成し
ており、この架橋の結合の力が表面張力に反映している
と考えられる。すなわち、酸素原子を介した架橋の力が
大きいほど、表面張力は大きいことになる。[0021] For example, in a melt of an oxide, unlike a solid in which atoms are regularly arranged and bonded, the atom is considered to have a higher degree of freedom, but on the surface of the liquid, it is bridged with another atom via an oxygen atom ( Dangle bond) is formed, and it is considered that the bonding force of this cross-link is reflected in the surface tension. That is, the greater the force of cross-linking via oxygen atoms, the greater the surface tension.
【0022】従って、岡邦彦,伊藤利充 低酸素分圧下
における銅酸化物単結晶育成.日本結晶成長学会紙,v
ol.21(1994) No.3 113に示される
ように、酸素の少ない雰囲気、還元雰囲気ほど、この酸
素原子による架橋を断ち切ることが可能となり、表面張
力を下げることが可能となる。言い換えれば、融液の結
晶成長においては雰囲気中の酸素濃度を変化させること
により融液の表面張力を変化させることが可能となると
言える。Therefore, Kunihiko Oka and Toshimitsu Ito have grown copper oxide single crystals under a low oxygen partial pressure. Japan Society for Crystal Growth, v
ol. 21 (1994) No. As shown in No. 3 113, in an atmosphere with less oxygen and in a reducing atmosphere, the cross-linking by the oxygen atoms can be cut off, and the surface tension can be lowered. In other words, it can be said that the surface tension of the melt can be changed by changing the oxygen concentration in the atmosphere during crystal growth of the melt.
【0023】そこで本発明者等は鋭意検討を進めた結
果、Fz法においても、雰囲気ガス中の酸素濃度を変化
させることにより溶融帯の表面張力を変化させることが
可能で、酸素濃度を高くすることにより溶融帯の表面張
力を高めれば、溶融帯の垂れが起こり難くなることから
上述のような肩部が容易に形成されることを見い出し
た。Therefore, as a result of intensive studies by the present inventors, even in the Fz method, the surface tension of the melting zone can be changed by changing the oxygen concentration in the atmosphere gas, and the oxygen concentration is increased. Therefore, it was found that if the surface tension of the melted zone is increased, sagging of the melted zone is less likely to occur, and thus the above-mentioned shoulder portion is easily formed.
【0024】また、Fz法においては溶融帯の量がCz
法と比較して非常に少ないことから表面張力を上げるこ
とにより攪拌効果が弱くなっても不都合は生じないこと
も見い出した。In the Fz method, the amount of the melting zone is Cz.
It was also found that there is no inconvenience even if the stirring effect is weakened by increasing the surface tension because it is much smaller than the method.
【0025】さらに、本発明者等は鋭意検討の結果、雰
囲気ガス中の酸素濃度、言い換えれば雰囲気ガス中の酸
素分圧が原料棒及び種結晶の融点を左右することを見い
出した。すなわち、相平衡の熱力学によるClausi
us−Claperonの式によれば、液相と固相が共
存する系において、圧力をp、温度をT、潜熱をL、液
体の体積をVL 、固体の体積をVS とすると、これらの
関係は下記式1のように表される。Further, as a result of intensive studies, the present inventors have found that the oxygen concentration in the atmosphere gas, in other words, the oxygen partial pressure in the atmosphere gas, influences the melting points of the raw material rod and the seed crystal. That is, Clausius by thermodynamics of phase equilibrium
According to the us-Claperon equation, in a system in which a liquid phase and a solid phase coexist, if pressure is p, temperature is T, latent heat is L, liquid volume is V L , and solid volume is V S , these The relationship is expressed by the following formula 1.
【0026】 dp/dT=L/T/(VL −VS )・・・(式1) また、上記式1から下記式2が導き出される。Dp / dT = L / T / (V L −V S ) ... (Equation 1) Further, the following Equation 2 is derived from the above Equation 1.
【0027】 dT=T/L・(VL −VS )・dp・・・(式2) 従って、雰囲気ガス中の酸素分圧を低くし、dp<0と
し、液体の体積が固体の体積よりも大きい材料系を使用
している場合、言い換えれば固体よりも液体の密度が小
さい場合、すなわち(VL −VS )>0であると、dT
<0となり、この材料系においては酸素分圧を下げると
融点が下がることがわかる。また、逆に酸素分圧を上げ
ると融点が上がることになる。水と氷の場合は逆となる
が、多くの系においては融点近傍では固体よりも液体の
方が密度が小さく、上記のように雰囲気ガス中の酸素分
圧を低くすると融点が下がる。[0027] dT = T / L · (V L -V S) · dp ··· ( Equation 2) Thus, to lower the oxygen partial pressure in the atmospheric gas, and dp <0, the volume volume of liquid is a solid If you are using larger material system than if the density of the liquid than solid in other words is small, i.e. is (V L -V S)> 0 , dT
It becomes <0, and it can be seen that the melting point is lowered in this material system when the oxygen partial pressure is lowered. Conversely, if the oxygen partial pressure is increased, the melting point will increase. In the case of water and ice, the opposite is true, but in many systems, the liquid has a lower density than the solid in the vicinity of the melting point, and the melting point decreases when the oxygen partial pressure in the atmosphere gas is lowered as described above.
【0028】すなわち本発明は、所定の雰囲気ガス中に
おいて原料棒及び/又は種結晶の先端部に溶融部を形成
し、原料棒と種結晶を接合してこれらの間に溶融帯を形
成し、この溶融帯を回転させながら前記原料棒内におい
て相対的に移動させることにより順次単結晶化してFz
法により単結晶を製造するに際し、原料棒と種結晶の接
合後、単結晶育成方向において次第に大径とされ、種結
晶よりも大径とされる肩部を形成し、続いて円筒状の直
胴部を形成することを特徴とするものである。That is, according to the present invention, a molten portion is formed at the tip of the raw material rod and / or the seed crystal in a predetermined atmosphere gas, the raw material rod and the seed crystal are joined to form a molten zone between them, By rotating the melting zone and relatively moving it in the raw material rod, the single crystal is sequentially formed into Fz.
When manufacturing a single crystal by the method, after joining the raw material rod and the seed crystal, the diameter of the shoulder is gradually increased in the single crystal growth direction to form a shoulder portion having a diameter larger than that of the seed crystal. It is characterized in that a body is formed.
【0029】そしてこのとき、原料棒と種結晶の接合後
から肩部形成までの雰囲気ガス中の酸素濃度をCo1 と
し、肩部形成時の雰囲気ガス中の酸素濃度をCo2 と
し、直胴部形成時の雰囲気ガス中の酸素濃度をCo3 と
した場合に、これらがCo1 =Co3 、Co1 ≦Co
2 、Co3 ≦Co2 の関係を有することが好ましく、肩
部形成時の酸素濃度を高めることにより溶融帯の垂れが
起こり難くなることから容易に肩部が形成されることと
なる。At this time, the oxygen concentration in the atmosphere gas from the joining of the raw material rod and the seed crystal to the formation of the shoulder portion is Co 1, and the oxygen concentration in the atmosphere gas when the shoulder portion is formed is Co 2. When the oxygen concentration in the atmosphere gas at the time of forming the portion is Co 3 , these are Co 1 = Co 3 , Co 1 ≦ Co
2 , it is preferable to have a relationship of Co 3 ≦ Co 2 , and by increasing the oxygen concentration at the time of forming the shoulder portion, sagging of the molten zone becomes difficult to occur, so that the shoulder portion is easily formed.
【0030】また、雰囲気ガス中の酸素濃度Co1 ,C
o2 ,Co3 が、1≦Co1 /Co2 ≦12.5、1≦
Co3 /Co2 ≦12.5の関係を有することが好まし
い。なお、上記のような酸素濃度の比が1未満である
と、肩部形成時の溶融帯の表面張力を高める効果が弱
く、上記のような酸素濃度の比が12.5よりも大であ
ると、肩部形成時の融点が高くなりすぎて単結晶の製造
が困難となる。Further, the oxygen concentrations Co 1 , C in the atmosphere gas
o 2 and Co 3 are 1 ≦ Co 1 / Co 2 ≦ 12.5, 1 ≦
It is preferable to have a relationship of Co 3 / Co 2 ≦ 12.5. If the oxygen concentration ratio as described above is less than 1, the effect of increasing the surface tension of the molten zone during shoulder formation is weak, and the oxygen concentration ratio as described above is greater than 12.5. Then, the melting point at the time of forming the shoulder portion becomes too high, which makes it difficult to manufacture a single crystal.
【0031】さらに本発明は、上述のようにFz法によ
り単結晶を製造するに際し、原料棒及び種結晶を融点近
傍における液体の密度が固体の密度よりも小さい材料系
により形成し、原料棒と種結晶の接合時の雰囲気ガス中
の酸素濃度(酸素分圧)を後工程における雰囲気ガス中
の酸素濃度(酸素分圧)よりも低くすることを特徴とす
るものである。Further, according to the present invention, when a single crystal is produced by the Fz method as described above, the raw material rod and the seed crystal are formed by a material system in which the liquid density near the melting point is smaller than the solid density to obtain the raw material rod. It is characterized in that the oxygen concentration (oxygen partial pressure) in the atmosphere gas at the time of joining the seed crystals is made lower than the oxygen concentration (oxygen partial pressure) in the atmosphere gas in the subsequent step.
【0032】さらにまた、本発明は、上述のようにFz
法により単結晶の製造を行うに際し、原料棒及び種結晶
を融点近傍における液体の密度が固体の密度よりも小さ
い材料系により形成し、原料棒と種結晶の接合時の雰囲
気ガス中の酸素濃度を後工程における雰囲気ガス中の酸
素濃度よりも低くするとともに、原料棒と種結晶の接合
後、単結晶育成方向において次第に大径とされ、種結晶
よりも大径とされる肩部を形成し、続いて円筒状の直胴
部を形成するようにしても良い。Furthermore, the present invention, as described above, uses Fz
When a single crystal is manufactured by the method, the raw material rod and the seed crystal are formed of a material system in which the density of the liquid near the melting point is smaller than the density of the solid, and the oxygen concentration in the atmosphere gas at the time of joining the raw material rod and the seed crystal. Is made lower than the oxygen concentration in the atmosphere gas in the post-process, and after joining the raw material rod and the seed crystal, the diameter is gradually increased in the single crystal growth direction to form a shoulder portion having a diameter larger than the seed crystal. Then, a cylindrical straight body portion may be formed subsequently.
【0033】本発明の単結晶の製造方法においては、F
z法により単結晶の製造を行うに際し、最終的には種結
晶よりも大径となる肩部を形成し、この上に直胴部を形
成することから、単結晶の大径化がなされる。そして、
このようにして単結晶を製造すれば、Fz法の利点を生
かした良質な単結晶が製造される。In the method for producing a single crystal of the present invention, F
When a single crystal is manufactured by the z method, a shoulder having a diameter larger than that of the seed crystal is finally formed, and a straight body is formed on the shoulder, so that the diameter of the single crystal is increased. . And
When a single crystal is manufactured in this manner, a high quality single crystal that takes advantage of the Fz method can be manufactured.
【0034】また、上記製造方法において、肩部形成時
の雰囲気ガス中の酸素濃度を高めれば、溶融帯の表面張
力が高くなり、溶融帯の垂れが起こり難くなり、肩部が
容易に形成される。Further, in the above manufacturing method, if the oxygen concentration in the atmosphere gas at the time of forming the shoulder portion is increased, the surface tension of the molten zone becomes high, the sag of the molten zone does not easily occur, and the shoulder portion is easily formed. It
【0035】さらに本発明の単結晶の製造方法において
は、Fz法により単結晶を製造するに際し、原料棒及び
種結晶を融点近傍における液体の密度が固体の密度より
も小さい材料系により形成し、原料棒と種結晶の接合時
の雰囲気ガス中の酸素濃度(酸素分圧)を後工程におけ
る雰囲気ガス中の酸素濃度(酸素分圧)よりも低くして
いるため、原料棒と種結晶の接合時のこれらの融点が低
くなり、これらの接合が容易となる。Further, in the method for producing a single crystal of the present invention, when producing a single crystal by the Fz method, the raw material rod and the seed crystal are formed of a material system in which the density of the liquid near the melting point is smaller than the density of the solid, Since the oxygen concentration (oxygen partial pressure) in the atmospheric gas at the time of joining the raw material rod and the seed crystal is lower than the oxygen concentration (oxygen partial pressure) in the atmospheric gas in the subsequent process, the joining of the raw material rod and the seed crystal is performed. At that time, their melting points are lowered, and they are easily joined.
【0036】[0036]
【発明の実施の形態】以下、本発明の具体的な実施の形
態について述べる。先ず、本発明の単結晶の製造方法に
より単結晶の製造を行うのに使用する単結晶製造装置に
ついて述べる。BEST MODE FOR CARRYING OUT THE INVENTION Specific embodiments of the present invention will be described below. First, a single crystal production apparatus used for producing a single crystal by the method for producing a single crystal of the present invention will be described.
【0037】上記単結晶製造装置は、図1に示すよう
に、赤外線集光加熱型育成炉2内に配される原料棒1a
と例えば種結晶1bが接する部分に、上記赤外線集光加
熱型育成炉2内に配される赤外線ランプ3,4の赤外線
を集光照射して溶融帯1cを形成し、上記原料棒1aを
所定の速さで図中下方に送り出す上部シャフト5と上記
種結晶1bを所定の速さで図中下方に引き下げる下部シ
ャフト6により原料棒1a及び種結晶1bを移動させる
ことにより溶融帯1cを原料棒1aの図中上方に相対的
に移動させて、溶融帯1c下端部を順次単結晶化して連
続的に単結晶を製造するものである。なお、上記単結晶
製造装置においては、種結晶1bの代わりに原料棒を用
いても良い。As shown in FIG. 1, the above-mentioned single crystal manufacturing apparatus has a raw material rod 1a arranged in an infrared converging heating type growth furnace 2.
For example, in the portion where the seed crystal 1b is in contact, the infrared rays of the infrared lamps 3 and 4 arranged in the infrared focusing heating type growth furnace 2 are focused and irradiated to form the melting zone 1c, and the raw material rod 1a is predetermined. The melted zone 1c is moved by moving the raw material rod 1a and the seed crystal 1b by the upper shaft 5 which sends out downward in the drawing at a speed of 5 and the lower shaft 6 which pulls down the seed crystal 1b at a predetermined speed downward in the drawing. 1a is relatively moved upward in the figure, and the lower end of the melting zone 1c is sequentially made into a single crystal to continuously produce a single crystal. In the above single crystal production apparatus, a raw material rod may be used instead of the seed crystal 1b.
【0038】上記赤外線集光加熱型育成炉2は、楕円の
一端部を切り欠いた略楕円形の断面の空洞部7a,7b
をそれぞれ有する炉体2a,2bが、上記空洞部7a,
7bを対向させるようにして突き合わされたものであ
る。そして、上記赤外線集光加熱型育成炉2内には、断
面が、2個の楕円の一方の焦点同士を重ねた形状、いわ
ゆる双楕円形の空洞部7が形成され、上記空洞部7の中
心は双楕円形の重ねた焦点となる。このとき、炉体2
a,2bの空洞部7a,7bの壁面が反射鏡となされて
いるため、空洞部7の壁面は双楕円面鏡となる。The infrared converging heating type growth furnace 2 has hollow portions 7a and 7b having a substantially elliptical cross section in which one end portion of an ellipse is cut out.
The furnace bodies 2a and 2b respectively having the
7b are opposed to each other. Then, in the infrared converging heating type growth furnace 2, a hollow portion 7 having a so-called bi-elliptical shape having a cross-section in which one of two ellipses' focal points are superposed is formed, and the center of the hollow portion 7 is formed. Is a bifocal, overlapping focus. At this time, the furnace body 2
Since the walls of the cavities 7a and 7b of a and 2b are reflection mirrors, the walls of the cavities 7 are bi-elliptical mirrors.
【0039】また、上記赤外線集光加熱型育成炉2には
その中央を貫通するように図中上下方向に延在する石英
管8が設けられており、該石英管8内の図中上下方向に
は雰囲気ガス流入口9と雰囲気ガス排気口10が設けら
れている。そして、雰囲気ガスの充填された石英管8内
において、原料棒1aは上部シャフト5、種結晶1bは
下部シャフト6により保持され、双楕円形の空洞部7の
中心、すなわち重ねた焦点上にこれらの接する部分が位
置するように配されている。The infrared converging heating type growth furnace 2 is provided with a quartz tube 8 extending vertically in the figure so as to penetrate the center thereof. Atmosphere gas inlet 9 and atmosphere gas exhaust port 10 are provided in the. In the quartz tube 8 filled with the atmospheric gas, the raw material rod 1a is held by the upper shaft 5 and the seed crystal 1b is held by the lower shaft 6, and these are placed at the center of the bi-elliptical cavity 7, that is, on the overlapping focus. Are arranged so that the contacting parts of are located.
【0040】さらに、上記上部シャフト5には駆動装置
11が接続され、原料棒1aを回転させながら図中下方
に送り出すことが可能とされており、下部シャフト6に
も駆動装置12が接続されて、種結晶1bを回転させな
がら図中下方に引き下げることが可能なようになされて
いる。Further, a drive device 11 is connected to the upper shaft 5 so that the raw material rod 1a can be fed downward in the drawing while rotating, and a drive device 12 is also connected to the lower shaft 6. The seed crystal 1b can be pulled down in the drawing while rotating.
【0041】なお、上部シャフト5の先端部には図示し
ない例えば白金線のフックが設けられて原料棒1aを保
持できるようになされ、下部シャフト6の先端部は図示
しない例えばアルミナのチューブで芯出しされて種結晶
1bを固定できるようになされているが、上部シャフト
5の先端部も同様の構成としても構わない。An unillustrated hook of, for example, a platinum wire is provided at the tip of the upper shaft 5 to hold the raw material rod 1a, and the tip of the lower shaft 6 is centered by an alumina tube (not shown). Although the seed crystal 1b is fixed by this, the tip portion of the upper shaft 5 may have the same structure.
【0042】そして、上記赤外線集光加熱型育成炉2の
炉体2a,2bの空洞部7a,7bの他方の焦点、すな
わち双楕円形の空洞部7の焦点にそれぞれ位置するよう
に一対の赤外線ランプ3,4が配されている。Then, a pair of infrared rays are positioned so as to be located at the other focal points of the cavity portions 7a, 7b of the furnace bodies 2a, 2b of the infrared converging heating type growth furnace 2, that is, at the focal points of the bi-elliptical cavity portions 7, respectively. Lamps 3 and 4 are arranged.
【0043】従って、双楕円形の空洞部7の焦点に位置
する一対の赤外線ランプ3,4から照射される赤外線
は、空洞部7壁面の双楕円面鏡により反射されて、原料
棒1aと種結晶1bの接する部分にあたる空洞部7の重
ねた焦点に位置する部分に必ず集光され、この部分が加
熱されて溶融帯1cとなる。なお、上記単結晶製造装置
においては、赤外線ランプ3,4として、ハロゲンラン
プを使用しているが、キセノンランプの使用も可能であ
る。Therefore, the infrared rays emitted from the pair of infrared lamps 3 and 4 located at the focal point of the bi-elliptical hollow portion 7 are reflected by the bi-elliptical mirror on the wall surface of the hollow portion 7 and seeded with the raw material rod 1a. The light is always focused on the overlapping focal point of the cavity 7 that is in contact with the crystal 1b, and this portion is heated to form the melting zone 1c. In the above single crystal manufacturing apparatus, halogen lamps are used as the infrared lamps 3 and 4, but xenon lamps can also be used.
【0044】また、上記赤外線集光加熱型育成炉2は、
炉体2a,2bを図中左右方向に移動させて開閉扉とし
て炉の開閉を可能とし、この開閉部から原料棒の取り付
け,取り外し、単結晶の取り出しを可能としている。The infrared condensing heating type growth furnace 2 is
The furnace bodies 2a and 2b are moved in the left-right direction in the figure to enable opening and closing of the furnace as an opening / closing door, and the raw material rods can be attached / detached and single crystals can be taken out from the opening / closing portion.
【0045】なお、上記単結晶製造装置においては、赤
外線集光加熱型育成炉2内部を観察できるように、該赤
外線集光加熱型育成炉2に図示しない観察用の窓が設け
られており、さらにこの観察用の窓に向けてレンズ1
3,フィルター14を介してビデオカメラ15が設けら
れている。In the above single crystal manufacturing apparatus, an observation window (not shown) is provided in the infrared converging heating type growth furnace 2 so that the inside of the infrared converging heating type growth furnace 2 can be observed. Lens 1 toward the observation window
A video camera 15 is provided via a filter 14.
【0046】従って、上記単結晶製造装置により本発明
の単結晶製造方法に従って単結晶の製造を行う場合に
は、先ず、所定の雰囲気ガスの充填された石英管8内に
おいて、上部シャフト5に原料棒を保持させるととも
に、下部シャフト6に種結晶を保持させる。Therefore, when a single crystal is manufactured by the above-described single crystal manufacturing apparatus according to the method for manufacturing a single crystal of the present invention, first, the raw material for the upper shaft 5 is placed in the quartz tube 8 filled with a predetermined atmosphere gas. While holding the rod, the lower shaft 6 holds the seed crystal.
【0047】次に、上部シャフト5,下部シャフト6に
保持された原料棒及び種結晶を逆方向に回転させ、例え
ば上部シャフト5に保持される原料棒の先端部に、一対
の赤外線ランプ3,4の赤外線を空洞部7の双楕円面鏡
により反射させて集光して照射し、上記先端部を加熱し
て溶融させ、メルトを形成する。Next, the raw material rod and the seed crystal held by the upper shaft 5 and the lower shaft 6 are rotated in the opposite direction, and, for example, a pair of infrared lamps 3, 3 are attached to the tip of the raw material rod held by the upper shaft 5. The infrared ray 4 is reflected by the bi-elliptical mirror of the cavity 7 and condensed and irradiated, and the above-mentioned tip is heated and melted to form a melt.
【0048】続いて、上部シャフト5に保持される原料
棒と下部シャフト6に保持される種結晶をメルトを介し
て接合させる。Then, the raw material rod held by the upper shaft 5 and the seed crystal held by the lower shaft 6 are joined together via the melt.
【0049】次に、上記石英管8内に所定の酸素濃度C
o1 の雰囲気ガスを充填し、この中で上記メルトを最初
の溶融帯とし、上部シャフト5及び下部シャフト6によ
り上記接合された原料棒と種結晶を所定の速さで逆方向
に回転させながら図中下方に引き下げて移動させること
により上記溶融帯1cを上部シャフト5側の原料棒1a
の図中上方に相対的に移動させ、溶融帯1cの下端部を
順次単結晶化する。Next, a predetermined oxygen concentration C is placed in the quartz tube 8.
while filling the atmosphere gas of o 1 with the above-mentioned melt as the first melting zone and rotating the raw material rod and the seed crystal joined by the upper shaft 5 and the lower shaft 6 in a reverse direction at a predetermined speed. The molten zone 1c is pulled down and moved downward in the figure to move the molten zone 1c to the raw material rod 1a on the upper shaft 5 side.
Of the melting zone 1c, the lower end of the melting zone 1c is sequentially made into a single crystal.
【0050】そして、上記石英管8内の雰囲気ガスを所
定の酸素濃度Co2 の雰囲気ガスに変える。このとき、
上記酸素濃度Co1 ,Co2 間には、Co1 ≦Co2 の
関係が成り立ち、1≦Co1 /Co2 ≦12.5である
ことが好ましく、1≦Co1/Co2 ≦7.5であるこ
とがより好ましい。Then, the atmospheric gas in the quartz tube 8 is changed to an atmospheric gas having a predetermined oxygen concentration Co 2 . At this time,
A relationship of Co 1 ≦ Co 2 is established between the oxygen concentrations Co 1 and Co 2 and preferably 1 ≦ Co 1 / Co 2 ≦ 12.5, and 1 ≦ Co 1 / Co 2 ≦ 7.5. Is more preferable.
【0051】このように雰囲気ガス中の酸素濃度を上げ
ると、溶融帯1cの表面張力が高まり溶融帯1cの垂れ
が起こり難くなることから、原料棒の送り込み速度を徐
々に速くし結晶径を徐々に大径とすることが可能であ
り、単結晶育成方向において次第に大径とされ、最終的
には種結晶よりも大径とされる肩部を形成することが可
能である。When the oxygen concentration in the atmosphere gas is increased in this way, the surface tension of the melting zone 1c increases and the sag of the melting zone 1c hardly occurs. Therefore, the feed rate of the raw material rod is gradually increased and the crystal diameter is gradually increased. It is possible to make the diameter larger and the diameter gradually becomes larger in the single crystal growth direction, and finally it is possible to form a shoulder portion having a larger diameter than the seed crystal.
【0052】なお、上記のように雰囲気ガス中の酸素濃
度を上げると、融点が高くなるため、溶融帯1cが固化
してくる可能性がある。そこで、上記のように酸素濃度
を上げる際には、赤外線ランプ3,4の出力も上げて溶
融帯の固化を防止するようにすることが好ましい。When the oxygen concentration in the atmosphere gas is increased as described above, the melting point is increased and the melting zone 1c may be solidified. Therefore, when increasing the oxygen concentration as described above, it is preferable to increase the outputs of the infrared lamps 3 and 4 to prevent the solidification of the melting zone.
【0053】また、雰囲気ガス中の酸素濃度Co1 ,C
o2 の比、Co1 /Co2 が1未満であると、肩部形成
時の溶融帯の表面張力を高める効果が弱く、上記のよう
な酸素濃度の比が12.5よりも大であると、肩部形成
時の融点が高くなりすぎて単結晶の製造が困難となる。Further, the oxygen concentration in the atmosphere gas Co 1 , C
If the ratio of O 2 is Co 1 / Co 2 is less than 1, the effect of increasing the surface tension of the molten zone at the time of shoulder formation is weak, and the above oxygen concentration ratio is larger than 12.5. Then, the melting point at the time of forming the shoulder portion becomes too high, which makes it difficult to manufacture a single crystal.
【0054】さらに、上記のように肩部を形成する前の
工程においては、原料棒1aの送り込み速度を遅くし、
径の細い単結晶を製造し、いわゆるネッキング部を形成
することが好ましく、上記のようなネッキング部を形成
した方が肩部の形成が容易となる。Further, in the step before forming the shoulder portion as described above, the feeding speed of the raw material rod 1a is decreased,
It is preferable to manufacture a single crystal having a small diameter to form a so-called necking portion, and the necking portion as described above facilitates formation of the shoulder portion.
【0055】また、これに伴い、順次単結晶化される原
料棒1aとしては、小径の原料棒と大径の原料棒が徐々
に大径となされる原料棒構成材料よりなる接続部を介し
て接続される原料棒を使用することが好ましく、小径の
原料棒により上記ネッキング部を形成し、接続部により
肩部を形成するようにすれば、上記のようなネッキング
部及び肩部の形成が容易となる。Along with this, as the raw material rods 1a which are successively single-crystallized, a small-diameter raw material rod and a large-diameter raw material rod are gradually increased in diameter through a connecting portion made of a raw material rod constituent material. It is preferable to use a raw material rod to be connected, and if the necking portion is formed by a raw material rod having a small diameter and the shoulder portion is formed by the connecting portion, it is easy to form the necking portion and the shoulder portion as described above. Becomes
【0056】次に、上記石英管8内の雰囲気ガス中の酸
素濃度を徐々に下げ、所定の酸素濃度Co2 まで下げる
とともに赤外線ランプ3,4の出力も徐々に下げ、上記
肩部の上に肩部の最上部と同等の直径の直胴部を形成す
る。このとき、上記酸素濃度Co2 ,Co3 間には、C
o3 ≦Co2 の関係が成り立ち、1≦Co3 /Co2≦
12.5であることが好ましく、1≦Co3 /Co2 ≦
7.5であることがより好ましい。Next, the oxygen concentration in the atmosphere gas in the quartz tube 8 is gradually lowered to a predetermined oxygen concentration Co 2 and the outputs of the infrared lamps 3 and 4 are gradually lowered so that the oxygen concentration in the atmosphere gas in the quartz tube 8 is lowered. A straight body part having the same diameter as the uppermost part of the shoulder part is formed. At this time, C is between the oxygen concentrations Co 2 and Co 3.
The relationship of o 3 ≦ Co 2 holds, and 1 ≦ Co 3 / Co 2 ≦
12.5 is preferable and 1 ≦ Co 3 / Co 2 ≦
It is more preferably 7.5.
【0057】また、雰囲気ガス中の酸素濃度Co2 ,C
o3 の比、Co3 /Co2 が1未満であると、肩部形成
時の溶融帯の表面張力を高める効果が弱く、上記のよう
な酸素濃度の比が12.5よりも大であると、肩部形成
時の融点が高くなりすぎて単結晶の製造が困難となる。Further, the oxygen concentration Co 2 and C in the atmosphere gas
When the ratio of o 3 is Co 3 / Co 2 is less than 1, the effect of increasing the surface tension of the molten zone at the time of shoulder formation is weak, and the above oxygen concentration ratio is larger than 12.5. Then, the melting point at the time of forming the shoulder portion becomes too high, which makes it difficult to manufacture a single crystal.
【0058】そして、連続的に単結晶を製造し、最終的
には上部シャフト5側の原料棒略全体を単結晶化すれ
ば、種結晶よりも大径となる肩部の上にこれと同径の直
胴部が形成されることから大型の単結晶が製造され、単
結晶の大型化がなされる。また、このようにして単結晶
を製造すればFz法の利点を生かした良質な単結晶が製
造される。Then, if a single crystal is continuously manufactured, and finally the material rod on the upper shaft 5 side is almost entirely made into a single crystal, the same is formed on the shoulder portion having a diameter larger than that of the seed crystal. Since the straight body portion having the diameter is formed, a large single crystal is manufactured, and the single crystal is enlarged. In addition, when a single crystal is manufactured in this manner, a high quality single crystal that makes the most of the advantages of the Fz method can be manufactured.
【0059】さらに、上記のようにして本発明の単結晶
の製造方法に従って単結晶を製造する際に、原料棒及び
種結晶を融点近傍における液体の密度が固体の密度より
も小さい材料系により形成し、原料棒と種結晶の接合時
の雰囲気ガス中の酸素濃度(酸素分圧)を後工程におけ
る雰囲気ガス中の酸素濃度(酸素分圧)よりも低くすれ
ば、原料棒と種結晶の接合時のこれらの融点が低くな
り、これらの接合が容易となる。また、上記のように接
合時の融点を低くすれば、加熱手段である赤外線ランプ
としてさほど高出力のものを必要とせず、集光度の高い
ものを使用できることから、単結晶の大径化の点におい
ても好ましい。Further, when a single crystal is produced according to the method for producing a single crystal of the present invention as described above, the raw material rod and the seed crystal are formed by a material system in which the liquid density near the melting point is smaller than the solid density. However, if the oxygen concentration (oxygen partial pressure) in the atmosphere gas when joining the raw material rod and the seed crystal is made lower than the oxygen concentration (oxygen partial pressure) in the atmosphere gas in the subsequent process, the joining of the raw material rod and the seed crystal is performed. At that time, their melting points are lowered, and they are easily joined. Further, if the melting point at the time of bonding is lowered as described above, an infrared lamp that is a heating means does not need to have a very high output and a highly focused light can be used. Is also preferable.
【0060】なお、このように原料棒と種結晶を接合す
る際に酸素濃度を低くし、その後工程ではそれ以上とす
る場合には、酸素濃度を上げると融点が高くなることか
ら酸素濃度を上げた直後において溶融帯が安定するまで
原料棒及び種結晶の回転方向を同方向とした方が良い。When the oxygen concentration is lowered when joining the raw material rod and the seed crystal in this way, and the oxygen concentration is increased in the subsequent step, the melting point becomes higher when the oxygen concentration is raised, so the oxygen concentration is raised. Immediately after that, it is preferable that the starting rod and the seed crystal rotate in the same direction until the melting zone becomes stable.
【0061】[0061]
【実施例】以下、本発明の具体的な実施例について実験
結果に基づいて説明する。なお、ここでは、YVO4 単
結晶を製造する例について述べる。EXAMPLES Hereinafter, specific examples of the present invention will be described based on experimental results. An example of producing a YVO 4 single crystal will be described here.
【0062】原料棒の作製 先ず、原料棒の作製を行った。最初に、純度4Nの酸化
イットリウム試薬(Y2 O3 )の灼熱減量を空気中で1
000℃×10時間で加熱処理して求め、純度4Nの酸
化バナジウム試薬(V2 O5 )の灼熱減量を空気中で5
00℃×10時間で加熱処理して求めた。そして、上記
Y2 O3 及びV2 O5 を1:1のモル比となるように秤
量した。Preparation of Raw Material Rod First, a raw material rod was manufactured. First, the ignition loss of yttrium oxide reagent (Y 2 O 3 ) having a purity of 4N was set to 1 in air.
Obtained by heating at 000 ° C. for 10 hours, and determine the ignition loss of vanadium oxide reagent (V 2 O 5 ) having a purity of 4N by 5 in air.
It was obtained by heat treatment at 00 ° C. for 10 hours. Then, the above Y 2 O 3 and V 2 O 5 were weighed so that the molar ratio was 1: 1.
【0063】次に、これらを分散媒としてエタノールを
用いて湿式混合して乾燥させて原料粉を作製した。そし
て、上記原料粉を直径が5〜8mm程度の袋状の生ゴム
(ラバーチューブ)内に充填し、これに静水圧3kg/
cm2 の圧力をかけて成形して原料棒とした。次に、こ
の原料棒を空気中で1300℃で6〜10時間程度焼成
し、原料棒サンプル1とした。得られた原料棒サンプル
1は、直径が約5mm程度で長さは50〜100mm程
度であった。Next, these were wet mixed using ethanol as a dispersion medium and dried to prepare a raw material powder. Then, the raw material powder was filled in a bag-shaped raw rubber (rubber tube) having a diameter of about 5 to 8 mm, and a hydrostatic pressure of 3 kg /
A material rod was formed by applying a pressure of cm 2 . Next, this raw material rod was fired in air at 1300 ° C. for about 6 to 10 hours to obtain raw material rod sample 1. The obtained raw material rod sample 1 had a diameter of about 5 mm and a length of about 50 to 100 mm.
【0064】また、上記原料粉を直径が5〜8mm程度
の小径部と直径が10mm程度の大径部が長さ5〜10
mmの円錐状の接続部を介して接続された袋状の生ゴム
(ラバーチューブ)内に充填し、これに静水圧3kg/
cm2 の圧力をかけて成形して原料棒とした。次に、こ
の原料棒を空気中で1300℃で6〜10時間程度焼成
し、原料棒サンプル2とした。得られた原料棒サンプル
2は、小径部の直径が約5mm程度で大径部の直径が8
〜9mm程度で、長さが100mm程度であった。In addition, the above raw material powder has a small diameter portion having a diameter of about 5 to 8 mm and a large diameter portion having a diameter of about 10 mm having a length of 5 to 10 mm.
It is filled in a bag-shaped raw rubber (rubber tube) connected via a conical connection part of mm, and a hydrostatic pressure of 3 kg /
A material rod was formed by applying a pressure of cm 2 . Next, this raw material rod was fired in air at 1300 ° C. for about 6 to 10 hours to obtain a raw material rod sample 2. In the obtained raw material rod sample 2, the diameter of the small diameter portion is about 5 mm and the diameter of the large diameter portion is 8 mm.
The length was about 9 mm and the length was about 100 mm.
【0065】実験例1 本実験例においては、雰囲気ガス中の酸素濃度と原料棒
及び種結晶の融点の関係を調査した。すなわち、本実験
例においては、雰囲気ガス中の酸素濃度を変化させ、そ
れぞれの条件下で原料棒を赤外線ランプにより加熱し、
原料棒が融け出す際の赤外線ランプの出力を調査し、雰
囲気ガス中の酸素濃度と赤外線ランプの出力の関係を調
査した。 Experimental Example 1 In this experimental example, the relationship between the oxygen concentration in the atmospheric gas and the melting points of the raw material rod and the seed crystal was investigated. That is, in this experimental example, the oxygen concentration in the atmosphere gas was changed, and the raw material rod was heated by an infrared lamp under each condition,
The output of the infrared lamp when the raw material rod melted was investigated, and the relationship between the oxygen concentration in the atmospheric gas and the output of the infrared lamp was investigated.
【0066】前述の構成の単結晶製造装置の赤外線ラン
プとして100V−1.5kWのランプを使用すること
とし、種結晶として〈001〉方位のYVO4 単結晶の
3〜4mm角で長さ20〜30mmのものを使用し、原
料棒として上記原料棒サンプル1のうちの長さ50mm
程度のものを使用した。A 100 V-1.5 kW lamp is used as the infrared lamp of the single crystal manufacturing apparatus having the above-mentioned structure, and the YVO 4 single crystal of <001> orientation is 3 to 4 mm square and has a length of 20 to 20 mm. A material rod of 30 mm is used, and the length of the raw material rod sample 1 is 50 mm.
Something was used.
【0067】なお、赤外線ランプとして1.5kWのも
のと3.5kWのものを用意し、これらの15V〜20
Vの電圧に相当する出力の時の集光領域を紙にあぶりだ
して確認したところ、1.5kWのものは直径5mmの
領域で集光され、3.5kWのものは直径10mmの領
域で集光された。集光領域が10mmではメルトの垂れ
が生じる可能性が高いことから集光領域が5mmの1.
5kWのものを使用することとした。Infrared lamps of 1.5 kW and 3.5 kW were prepared, and these 15 V to 20 V
When the light-collecting area at the time of output corresponding to the voltage of V was printed on the paper and confirmed, the light of 1.5 kW was collected in the area of 5 mm in diameter and the one of 3.5 kW was collected in the area of 10 mm in diameter. Was done. When the condensing area is 10 mm, it is highly possible that melt dripping occurs.
It was decided to use the one of 5 kW.
【0068】先ず、上記原料棒を単結晶製造装置の上部
シャフトにフックにより保持させ、種結晶を下部シャフ
トにアルミナよりなるチューブで芯出しして保持させ
た。次に、前述の構成の単結晶製造装置の石英管内に所
定の雰囲気ガスを充填させた。First, the above raw material rod was held on the upper shaft of the single crystal manufacturing apparatus by a hook, and the seed crystal was centered and held on the lower shaft by a tube made of alumina. Next, a predetermined atmosphere gas was filled in the quartz tube of the single crystal manufacturing apparatus having the above-described structure.
【0069】前述の構成の単結晶製造装置においては、
排気装置が設けられていないことから、石英管内の空気
を完全に排気して所定の雰囲気ガスに置換することは不
可能である。そこで、雰囲気ガス流入口と雰囲気ガス流
出口を通じて所定の雰囲気ガスを終夜流通させることに
より、置換を行い、充填させることとした。In the single crystal manufacturing apparatus having the above-mentioned structure,
Since no exhaust device is provided, it is impossible to completely exhaust the air in the quartz tube and replace it with a predetermined atmospheric gas. Therefore, a predetermined atmosphere gas is allowed to flow overnight through the atmosphere gas inlet and the atmosphere gas outlet to perform replacement and filling.
【0070】上記雰囲気ガスとしては、窒素ガスを毎分
2.5リットルと酸素ガスを毎分0〜0.6リットルの
範囲で変化させた酸素濃度0〜20%のガスを使用し
た。このとき、石英管内は十分に時間をかけて雰囲気ガ
スにより置換されているため、上記のように流量の割合
で酸素濃度を表すものとした。As the atmosphere gas, a gas having an oxygen concentration of 0 to 20% was used, in which nitrogen gas was changed to 2.5 liters per minute and oxygen gas was changed to 0 to 0.6 liters per minute. At this time, since the inside of the quartz tube is sufficiently replaced with the atmospheric gas, the oxygen concentration is represented by the flow rate as described above.
【0071】続いて、上記原料棒を6.5rpmの回転
速度で回転させ、上記種結晶を6rpmの回転速度で反
対方向に回転させ、原料棒の先端に上記赤外線ランプの
光を照射した。Subsequently, the raw material rod was rotated at a rotation speed of 6.5 rpm, the seed crystal was rotated in the opposite direction at a rotation speed of 6 rpm, and the tip of the raw material rod was irradiated with light from the infrared lamp.
【0072】赤外線ランプの出力制御は電圧制御により
行うものとし、1つのプログラム計で2つの赤外線ラン
プの出力制御を行うものとした。そして、赤外線ランプ
の出力を原料棒が融け始めると思われる電圧近傍までプ
ログラムを使用して自動的に上げ、次に原料棒が融け始
めるまで手動で上げていくこととし、このときの赤外線
ランプの出力を調査するとともに溶融帯の固液界面の幅
が4mmになったときの赤外線ランプの出力も調査し
た。酸素濃度と赤外線ランプの出力の関係を表1に示
し、原料棒が融け始めた時(融点)の赤外線ランプの出
力をPw1 、固液界面の幅が4mmになったときの赤外
線ランプの出力をPw2 として示す。また、酸素濃度と
赤外線ランプの出力Pw2 の関係は図2にも示す。The output control of the infrared lamp is performed by voltage control, and the output control of the two infrared lamps is performed by one program meter. Then, the output of the infrared lamp is automatically increased by using a program up to the voltage near the point where the raw material rod starts to melt, and then it is manually increased until the raw material rod begins to melt. The output was also investigated and the output of the infrared lamp when the width of the solid-liquid interface of the melting zone was 4 mm was also investigated. The relationship between the oxygen concentration and the output of the infrared lamp is shown in Table 1. The output of the infrared lamp when the raw material bar starts to melt (melting point) is Pw 1 , and the output of the infrared lamp when the solid-liquid interface width is 4 mm. Is shown as Pw 2 . The relationship between the oxygen concentration and the output Pw 2 of the infrared lamp is also shown in FIG.
【0073】[0073]
【表1】 [Table 1]
【0074】表1及び図2の結果から雰囲気ガス中の酸
素濃度が低いほど、原料棒が溶融するとき、溶融帯の固
液界面の幅が4mmになったときの赤外線ランプの出力
が小さいことがわかる。From the results of Table 1 and FIG. 2, the lower the oxygen concentration in the atmospheric gas, the smaller the output of the infrared lamp when the raw material rod is melted and the width of the solid-liquid interface in the melting zone is 4 mm. I understand.
【0075】また、上記赤外線ランプの出力と集光部に
おける温度の関係を図3に示す。図3から赤外線ランプ
の出力が大きいほど集光部の温度が高くなることがわか
る。FIG. 3 shows the relationship between the output of the infrared lamp and the temperature at the condensing part. It can be seen from FIG. 3 that the higher the output of the infrared lamp, the higher the temperature of the condensing part.
【0076】従って、これらのことから、雰囲気ガス中
の酸素濃度を低くすると原料棒の融点が低くなることが
確認され、原料棒と種結晶の接合時の雰囲気ガス中の酸
素濃度を低くすれば、これらの接合が容易となることも
わかった。さらには、接合時の雰囲気ガス中の酸素濃度
を低くすることで、このときの赤外線ランプの出力を小
さく抑えることが可能であることから、赤外線ランプと
してさほど出力の大きなものは必要なく、単結晶の大径
化の点からも好ましいことがわかった。Therefore, from these facts, it was confirmed that when the oxygen concentration in the atmosphere gas is lowered, the melting point of the raw material rod is lowered, and when the oxygen concentration in the atmosphere gas at the time of joining the raw material rod and the seed crystal is lowered. , It was also found that these can be easily joined. Furthermore, by lowering the oxygen concentration in the atmosphere gas at the time of bonding, the output of the infrared lamp at this time can be suppressed to a small value, so there is no need for an infrared lamp with a large output, and a single crystal It was found that it is also preferable from the viewpoint of increasing the diameter.
【0077】実験例2 本実験例においては、YVO4 単結晶の製造例を示す。
先ず、前述の構成の単結晶製造装置の石英管内に前述の
直径5mm程度の小径部の長さが5〜10mm程度で直
径8〜9mm程度の大径部の長さが50mm程度の原料
棒サンプル2を上部シャフトの白金線のフックにより保
持し、〈100〉方位のYVO4 単結晶の3〜4mm角
で長さが20〜30mmの種結晶を下部シャフトのアル
ミナのチューブに芯出しして保持した。 Experimental Example 2 In this Experimental Example, an example of producing a YVO 4 single crystal is shown.
First, a raw material rod sample in which the length of the small diameter portion having a diameter of about 5 mm is about 5 to 10 mm and the length of the large diameter portion having a diameter of about 8 to 9 mm is about 50 mm in the quartz tube of the single crystal manufacturing apparatus having the above-described configuration. 2 is held by a platinum wire hook on the upper shaft, and a seed crystal of YVO 4 single crystal of <100> orientation with a 3 to 4 mm square and a length of 20 to 30 mm is centered and held on the alumina tube of the lower shaft. did.
【0078】そして、石英管内に窒素ガスを毎分2.5
リットル近傍で終夜流通させ、石英管内を窒素ガスによ
り置換し、充填した。Then, nitrogen gas is fed into the quartz tube at a rate of 2.5 per minute.
It was circulated overnight in the vicinity of liter, and the inside of the quartz tube was replaced with nitrogen gas and filled.
【0079】次に、原料棒を回転速度6.5rpmで回
転させるとともに種結晶を回転速度6rpmで逆方向に
回転させ、原料棒の先端部に赤外線ランプの光を集光照
射した。なお、上記赤外線ランプとしては100V−
1.5kWの赤外線ランプを使用することとし、ランプ
の出力制御は電圧により行うものとし、1つのプログラ
ム計で2つの赤外線ランプの制御を行うことにした。Next, the raw material rod was rotated at a rotation speed of 6.5 rpm and the seed crystal was rotated in the opposite direction at a rotation speed of 6 rpm, and the light from the infrared lamp was focused and irradiated onto the tip of the raw material rod. The infrared lamp is 100 V-
It was decided to use an infrared lamp of 1.5 kW, and to control the output of the lamp by voltage, and to control two infrared lamps with one program meter.
【0080】そして、上記プログラム計により、赤外線
ランプの電圧を原料棒が融け始めると思われる出力に対
応する電圧に近い60V(1.3kW)まで2時間程度
かけて自動的に上げて集光部分の温度を昇温させ、次に
手動操作により電圧を上げ、原料棒先端部を溶融させて
メルトを形成し、これを溶融帯として介して原料棒と種
結晶を接合した。このときの電圧は64V(1.4k
W)前後であった。Then, the program meter automatically raises the voltage of the infrared lamp to 60 V (1.3 kW), which is close to the voltage corresponding to the output at which the raw material bar starts to melt, for about 2 hours to automatically collect the light. The temperature was raised, and then the voltage was increased by manual operation to melt the tip of the raw material rod to form a melt, and the raw material rod and the seed crystal were joined via this as a melting zone. The voltage at this time is 64V (1.4k
W) was around.
【0081】なお、上記のように原料棒と種結晶を接合
する際、特願平6−16853号明細書に記載されるよ
うに、原料棒と種結晶の接する部分を、酸素を含み、バ
ナジウムとイットリウムの組成比をV/Yとすると、上
記V/Yが0.8≦V/Y≦1.25である組成を有
し、波長0.4μm以上,1.3μm以下の帯域に吸収
を有する黒色物質としても良い。When joining the raw material rod and the seed crystal as described above, as described in Japanese Patent Application No. 6-16853, the portion where the raw material rod and the seed crystal contact each other contains oxygen and vanadium. If the composition ratio of yttrium and yttrium is V / Y, the above V / Y has a composition of 0.8 ≦ V / Y ≦ 1.25 and absorbs light in the wavelength band of 0.4 μm or more and 1.3 μm or less. The black substance may be included.
【0082】次に、原料棒と種結晶を同方向に回転速度
6rpmで回転させ、雰囲気ガス中の酸素濃度Co1 を
0.8%とした。このように酸素濃度を上げると、溶融
帯の融点が上がり一部が固化して溶融帯が不安定となる
可能性があるため、上記のように原料棒と種結晶を同方
向に回転させることとした。続いて、上記溶融帯の固液
界面の幅が4mm程度となるまで赤外線ランプの電圧を
上げた。このときの電圧は68〜70V(1.5〜1.
7kW)程度であった。Next, the raw material rod and the seed crystal were rotated in the same direction at a rotation speed of 6 rpm to adjust the oxygen concentration Co 1 in the atmospheric gas to 0.8%. If the oxygen concentration is increased in this way, the melting point of the melting zone rises and some of it may solidify, making the melting zone unstable.Therefore, rotate the raw material rod and the seed crystal in the same direction as described above. And Subsequently, the voltage of the infrared lamp was increased until the width of the solid-liquid interface of the melting zone became about 4 mm. The voltage at this time is 68 to 70 V (1.5 to 1.
It was about 7 kW).
【0083】次に、原料棒を回転速度を6.5rpmと
して回転させ、種結晶を回転速度を6rpmとして反対
方向に回転させながら原料棒を下部シャフト側に送り出
し、溶融帯を原料棒中で相対的に移動させ、溶融帯下端
部を順次単結晶化して単結晶を製造した。ただし、この
とき、単結晶の育成速度を5.0mm/時とし、原料棒
の送り出し速度を3.9mm/時から3.4mm/時ま
で徐々に遅くして単結晶の径を細くし、いわゆるネッキ
ング部を長さ5〜10mm程度に形成した。Next, the raw material rod is rotated at a rotation speed of 6.5 rpm, the seed crystal is fed to the lower shaft side while rotating the seed crystal in the opposite direction at a rotation speed of 6 rpm, and the melting zone is relatively moved in the raw material rod. And the lower end of the melting zone was sequentially made into a single crystal to produce a single crystal. However, at this time, the growth rate of the single crystal was set to 5.0 mm / hour, and the feed rate of the raw material rod was gradually decreased from 3.9 mm / hour to 3.4 mm / hour to reduce the diameter of the single crystal. The necking portion was formed to have a length of about 5 to 10 mm.
【0084】次に、石英管内の雰囲気ガス中の酸素濃度
を上げながら赤外線ランプの出力も上げて原料棒の送り
出し速度を速め、結晶径を徐々に大径とし、単結晶育成
方向において次第に大径とされ、最終的には種結晶より
も大径とされる肩部を形成した。単に雰囲気ガス中の酸
素濃度を上げると、溶融帯の融点が上がり一部が固化し
て溶融帯が不安定となる可能性があるため、溶融帯の固
液界面の幅を一定に保てるように赤外線ランプの電圧も
上げた。酸素濃度は肩部形成工程の8割程度までかけて
徐々に上昇させるものとし、最終的な酸素濃度Co2 は
10%とした。すなわち、Co1 ≦Co2 であり、Co
1 /Co2 =12.5である。また、原料棒の送り出し
速度は7.5mm/時まで上げた。Next, while increasing the oxygen concentration in the atmosphere gas in the quartz tube, the output of the infrared lamp was also increased to increase the feed rate of the raw material rod to gradually increase the crystal diameter and gradually increase the diameter in the single crystal growth direction. And finally formed a shoulder having a diameter larger than that of the seed crystal. If the oxygen concentration in the atmosphere gas is simply increased, the melting point of the melting zone rises and some of it may solidify, making the melting zone unstable, so keep the width of the solid-liquid interface in the melting zone constant. The voltage of the infrared lamp was also raised. The oxygen concentration was gradually increased up to about 80% of the shoulder forming step, and the final oxygen concentration Co 2 was 10%. That is, Co 1 ≦ Co 2 , and Co
1 / Co 2 = 12.5. Further, the feed rate of the raw material rod was increased to 7.5 mm / hour.
【0085】次に、肩部形成工程の残り2割において、
溶融帯の固液界面の幅が一定となるようにランプの電圧
を下げながら酸素濃度も除々に下げ、酸素濃度Co3 が
0.8%となるように下げた。そして原料棒の送り込み
速度を7.5mm/時とし、上記肩部の上に肩部の最上
部と同等の直径の直胴部を形成した。このとき、上記酸
素濃度Co2 ,Co3 間には、Co3 ≦Co2 の関係が
成り立ち、Co3 /Co2 =12.5である。得られた
直胴部は直径9mm程度で長さが30〜50mm程度の
ものであった。Next, in the remaining 20% of the shoulder forming process,
The oxygen concentration was gradually lowered while lowering the voltage of the lamp so that the width of the solid-liquid interface of the melting zone was constant, and the oxygen concentration Co 3 was lowered to 0.8%. Then, the feed rate of the raw material rod was set to 7.5 mm / hour, and a straight body portion having the same diameter as the uppermost portion of the shoulder portion was formed on the shoulder portion. At this time, the relationship of Co 3 ≦ Co 2 is established between the oxygen concentrations Co 2 and Co 3 , and Co 3 / Co 2 = 12.5. The obtained straight body part had a diameter of about 9 mm and a length of about 30 to 50 mm.
【0086】本実験例においては、酸素濃度Co1 ,C
o3 を0.8%としているが、これは酸素濃度を比較的
低くして融点を下げるためと、バナジウムの蒸気圧が高
いのでその蒸散を抑えるためである。In this experimental example, the oxygen concentrations Co 1 , C
Although o 3 is 0.8%, this is because the oxygen concentration is relatively low to lower the melting point, and because the vapor pressure of vanadium is high, its evaporation is suppressed.
【0087】そして、このようにして得られた単結晶に
おいては、最終的には種結晶よりも大径となる肩部の上
に直胴部を形成することから、単結晶の大径化がなされ
るとともに、Fz法の利点を生かした良質な特性を有す
ることが確認された。In the single crystal thus obtained, since the straight body is finally formed on the shoulder portion having a larger diameter than that of the seed crystal, it is possible to increase the diameter of the single crystal. In addition, it was confirmed that it has good quality characteristics that make use of the advantages of the Fz method.
【0088】実験例3 この他、本発明者等は原料棒として原料棒サンプル1を
使用して酸素濃度を0.8%の一定に保って単結晶の製
造を行ってみたが、メルトが垂れないような原料棒の送
り出し速度は4mm/時程度であり、肩部の形成は難し
いことが確認された。また、得られた単結晶の直径も4
〜6mm程度であり、単結晶の大型化には対応困難であ
ることも確認された。 Experimental Example 3 In addition, the inventors of the present invention used the raw material rod sample 1 as a raw material rod to manufacture a single crystal while keeping the oxygen concentration constant at 0.8%. It was confirmed that the feed rate of the raw material bar that does not exist was about 4 mm / hour, and that it was difficult to form the shoulder portion. Also, the diameter of the obtained single crystal is 4
It was about 6 mm, and it was also confirmed that it was difficult to cope with an increase in the size of a single crystal.
【0089】さらに、原料棒の径が大きいことから原料
棒への赤外線ランプの照射密度が低くなり、メルトの形
成が難しく、赤外線ランプの電圧が80V程度となって
もメルトが形成されず、84Vと高電圧下で突然メルト
が形成されて垂れる等のトラブルが発生した。Furthermore, since the diameter of the raw material rod is large, the irradiation density of the infrared lamp on the raw material rod is low, and it is difficult to form a melt. Even if the voltage of the infrared lamp reaches about 80V, no melt is formed and 84V is used. Then, a problem such as sudden melt formation under high voltage and dripping occurred.
【0090】これらのことから、酸素濃度を変化させず
に肩部の形成を行う、或いは原料棒と種結晶の接合を行
うのは困難であることが確認された。From the above, it was confirmed that it is difficult to form the shoulder portion or to join the raw material rod and the seed crystal without changing the oxygen concentration.
【0091】実験例4 また、本発明者等は、肩部形成時に溶融帯が垂れないた
めの酸素濃度の範囲についても調査した。その結果、3
%以上、12%以下、好ましくは6%以下であることが
わかった。すなわち、雰囲気ガス中の酸素濃度Co1 ,
Co2 ,Co3が、1≦Co1 /Co2 ≦12.5、1
≦Co3 /Co2 ≦12.5、好ましくは1≦Co1 /
Co2 ≦7.5、1≦Co3 /Co2 ≦7.5であれ
ば、溶融帯の垂れが起こらないことが確認された。 Experimental Example 4 The present inventors also investigated the range of oxygen concentration for preventing the molten zone from sagging when forming the shoulder. As a result, 3
It was found that the content is not less than% and not more than 12%, preferably not more than 6%. That is, the oxygen concentration Co 1 in the atmosphere gas,
Co 2 and Co 3 are 1 ≦ Co 1 / Co 2 ≦ 12.5, 1
≦ Co 3 / Co 2 ≦ 12.5, preferably 1 ≦ Co 1 /
If Co 2 ≦ 7.5,1 ≦ Co 3 / Co 2 ≦ 7.5, it was confirmed that the dripping of the molten zone does not occur.
【0092】[0092]
【発明の効果】以上の説明からも明らかなように、本発
明の単結晶の製造方法においては、Fz法により単結晶
の製造を行うに際し、最終的には種結晶よりも大径とな
る肩部の上にそのまま直胴部を形成することから、単結
晶の大径化がなされる。そして、このようにして単結晶
を製造すれば、Fz法の利点を生かした良質な単結晶が
製造される。As is apparent from the above description, in the method for producing a single crystal according to the present invention, when the single crystal is produced by the Fz method, the diameter of the shoulder finally becomes larger than that of the seed crystal. Since the straight body portion is formed on the portion as it is, the diameter of the single crystal is increased. When a single crystal is manufactured in this manner, a good quality single crystal that makes the most of the advantages of the Fz method is manufactured.
【0093】また、上記製造方法において、肩部形成時
の雰囲気ガス中の酸素濃度を高めれば、溶融帯の表面張
力が高くなり、溶融帯の垂れが起こり難くなり、肩部が
容易に形成される。Further, in the above manufacturing method, if the oxygen concentration in the atmosphere gas at the time of forming the shoulder portion is increased, the surface tension of the molten zone becomes high, the sagging of the molten zone does not easily occur, and the shoulder portion is easily formed. It
【0094】さらに本発明の単結晶の製造方法において
は、Fz法により単結晶を製造するに際し、原料棒及び
種結晶を融点近傍における液体の密度が固体の密度より
も小さい材料系により形成し、原料棒と種結晶の接合時
の雰囲気ガス中の酸素濃度を後工程における雰囲気ガス
中の酸素濃度よりも低くしているため、原料棒と種結晶
の接合時のこれらの融点が低くなり、これらの接合が容
易となる。また、上記のように接合時の融点を低くすれ
ば、加熱手段として例えば赤外線ランプ等を使用した場
合においてもさほど高出力のものを必要とせず、結晶の
大径化の点からも好ましい。Further, in the method for producing a single crystal of the present invention, when producing a single crystal by the Fz method, the raw material rod and the seed crystal are formed of a material system in which the density of the liquid near the melting point is smaller than the density of the solid, Since the oxygen concentration in the atmosphere gas at the time of joining the raw material rod and the seed crystal is made lower than the oxygen concentration in the atmosphere gas in the subsequent step, the melting point of these at the time of joining the raw material rod and the seed crystal becomes low, Will be easy to join. Further, if the melting point at the time of joining is lowered as described above, even when an infrared lamp or the like is used as the heating means, a high output is not required, and it is preferable from the viewpoint of increasing the crystal diameter.
【図1】単結晶製造装置の一構成例を模式的に示す断面
図である。FIG. 1 is a cross-sectional view schematically showing a configuration example of a single crystal manufacturing apparatus.
【図2】酸素濃度と赤外線ランプの出力Pw2 の関係を
示す特性図である。FIG. 2 is a characteristic diagram showing the relationship between oxygen concentration and infrared lamp output Pw 2 .
【図3】赤外線ランプの出力と集光部における温度の関
係を示す特性図である。FIG. 3 is a characteristic diagram showing the relationship between the output of the infrared lamp and the temperature at the condensing part.
1a 原料棒 1b 種結晶 1c 溶融帯 2 赤外線集光加熱型育成炉 3,4 赤外線ランプ 5 上部シャフト 6 下部シャフト 7 空洞部 1a Raw material rod 1b Seed crystal 1c Melting zone 2 Infrared focusing heating type growth furnace 3,4 Infrared lamp 5 Upper shaft 6 Lower shaft 7 Cavity
Claims (5)
/又は種結晶の先端部に溶融部を形成し、原料棒と種結
晶を接合してこれらの間に溶融帯を形成し、この溶融帯
を回転させながら前記原料棒内において相対的に移動さ
せることにより順次単結晶化して単結晶を製造する単結
晶の製造方法において、 原料棒と種結晶の接合後、単結晶育成方向において次第
に大径とされ、種結晶よりも大径とされる肩部を形成
し、続いて円筒状の直胴部を形成することを特徴とする
単結晶の製造方法。1. A molten zone is formed at a tip of a raw material rod and / or a seed crystal in a predetermined atmosphere gas, a raw material rod and a seed crystal are joined to form a molten zone between them, and the molten zone is formed. In the method for producing a single crystal in which a single crystal is produced by sequentially moving the raw material rod into a single crystal while rotating the raw material rod, a large diameter gradually increases in the single crystal growth direction after joining the raw material rod and the seed crystal. And forming a shoulder portion having a diameter larger than that of the seed crystal, and then forming a cylindrical straight body portion.
での雰囲気ガス中の酸素濃度をCo1 とし、肩部形成時
の雰囲気ガス中の酸素濃度をCo2 とし、直胴部形成時
の雰囲気ガス中の酸素濃度をCo3 とした場合に、これ
らがCo1 =Co3 、Co1 ≦Co2 、Co3 ≦Co2
の関係を有することを特徴とする請求項1記載の単結晶
の製造方法。2. The straight body portion is formed by setting the oxygen concentration in the atmosphere gas from the joining of the raw material rod and the seed crystal to the shoulder formation to Co 1 and the oxygen concentration in the atmosphere gas when forming the shoulder portion to Co 2. When the oxygen concentration in the atmosphere gas at this time is Co 3 , these are Co 1 = Co 3 , Co 1 ≤Co 2 , Co 3 ≤Co 2
The method for producing a single crystal according to claim 1, having the following relationship.
2 ,Co3 が、1≦Co1 /Co2 ≦12.5、1≦C
o3 /Co2 ≦12.5の関係を有することを特徴とす
る請求項2記載の単結晶の製造方法。3. Oxygen concentration Co 1 , Co in the atmosphere gas
2 , Co 3 is 1 ≦ Co 1 / Co 2 ≦ 12.5, 1 ≦ C
The method for producing a single crystal according to claim 2, having a relationship of o 3 / Co 2 ≦ 12.5.
/又は種結晶の先端部に溶融部を形成し、原料棒と種結
晶を接合してこれらの間に溶融帯を形成し、この溶融帯
を回転させながら前記原料棒内において相対的に移動さ
せることにより順次単結晶化して単結晶を製造する単結
晶の製造方法において、 原料棒及び種結晶を融点近傍における液体の密度が固体
の密度よりも小さい材料系により形成し、原料棒と種結
晶の接合時の雰囲気ガス中の酸素濃度を後工程における
雰囲気ガス中の酸素濃度よりも低くすることを特徴とす
る単結晶の製造方法。4. A molten zone is formed at the tip of a raw material rod and / or a seed crystal in a predetermined atmosphere gas, a raw material rod and a seed crystal are joined to form a molten zone between them, and this molten zone is formed. In the method for producing a single crystal in which a single crystal is sequentially produced by sequentially moving the raw material rod while rotating the raw material rod, the density of the liquid near the melting point of the raw material rod and the seed crystal is higher than that of the solid. And the oxygen concentration in the atmosphere gas at the time of joining the raw material rod and the seed crystal are made lower than the oxygen concentration in the atmosphere gas in the subsequent step.
/又は種結晶の先端部に溶融部を形成し、原料棒と種結
晶を接合してこれらの間に溶融帯を形成し、この溶融帯
を回転させながら前記原料棒内において相対的に移動さ
せることにより順次単結晶化して単結晶を製造する単結
晶の製造方法において、 原料棒及び種結晶を融点近傍における液体の密度が固体
の密度よりも小さい材料系により形成し、原料棒と種結
晶の接合時の雰囲気ガス中の酸素濃度を後工程における
雰囲気ガス中の酸素濃度よりも低くするとともに、原料
棒と種結晶の接合後、単結晶育成方向において次第に大
径とされ、種結晶よりも大径とされる肩部を形成し、続
いて円筒状の直胴部を形成することを特徴とする単結晶
の製造方法。5. A melting zone is formed at the tip of a raw material rod and / or a seed crystal in a predetermined atmosphere gas, a raw material rod and a seed crystal are joined to form a melting zone between them, and the melting zone is formed. In the method for producing a single crystal in which a single crystal is sequentially produced by sequentially moving the raw material rod while rotating the raw material rod, the density of the liquid near the melting point of the raw material rod and the seed crystal is higher than that of the solid. Is formed from a small material system, the oxygen concentration in the atmosphere gas at the time of joining the raw material rod and the seed crystal is made lower than the oxygen concentration in the atmosphere gas in the subsequent process, and after joining the raw material rod and the seed crystal, a single crystal is formed. A method for producing a single crystal, which comprises forming a shoulder portion having a diameter gradually increasing in a growing direction and having a diameter larger than that of a seed crystal, and then forming a cylindrical straight body portion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19336495A JP3557734B2 (en) | 1995-07-28 | 1995-07-28 | Single crystal manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19336495A JP3557734B2 (en) | 1995-07-28 | 1995-07-28 | Single crystal manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0940486A true JPH0940486A (en) | 1997-02-10 |
| JP3557734B2 JP3557734B2 (en) | 2004-08-25 |
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ID=16306691
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|---|---|---|---|
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| Country | Link |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003332657A (en) * | 2002-05-17 | 2003-11-21 | Megaopto Co Ltd | Laser system |
-
1995
- 1995-07-28 JP JP19336495A patent/JP3557734B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003332657A (en) * | 2002-05-17 | 2003-11-21 | Megaopto Co Ltd | Laser system |
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| Publication number | Publication date |
|---|---|
| JP3557734B2 (en) | 2004-08-25 |
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