JPH062637B2 - Single crystal pulling device - Google Patents

Single crystal pulling device

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Publication number
JPH062637B2
JPH062637B2 JP62174398A JP17439887A JPH062637B2 JP H062637 B2 JPH062637 B2 JP H062637B2 JP 62174398 A JP62174398 A JP 62174398A JP 17439887 A JP17439887 A JP 17439887A JP H062637 B2 JPH062637 B2 JP H062637B2
Authority
JP
Japan
Prior art keywords
single crystal
ppm
ash content
graphite
crucible
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.)
Expired - Lifetime
Application number
JP62174398A
Other languages
Japanese (ja)
Other versions
JPS6418986A (en
Inventor
照久 近藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyo Tanso Co Ltd
Original Assignee
Toyo Tanso Co Ltd
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Filing date
Publication date
Application filed by Toyo Tanso Co Ltd filed Critical Toyo Tanso Co Ltd
Priority to JP62174398A priority Critical patent/JPH062637B2/en
Publication of JPS6418986A publication Critical patent/JPS6418986A/en
Publication of JPH062637B2 publication Critical patent/JPH062637B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は単結晶引上装置に関し、特に半導体用単結晶引
上装置に関する。
The present invention relates to a single crystal pulling apparatus, and more particularly to a single crystal pulling apparatus for semiconductors.

〔従来の技術〕[Conventional technology]

単結晶引上装置就中半導体用単結晶引上装置としてその
代表的なものにシリコン単結晶引上装置があり、その他
ガリウム系例えばGa-As系、Ga-P系の単結晶引上装置が
ある。いまこれ等を代表してシリコン単結晶引上装置に
ついて説明する。
Single crystal pulling device Among others, a silicon single crystal pulling device is a typical one as a semiconductor single crystal pulling device, and other gallium-based, for example, Ga-As-based or Ga-P-based single crystal pulling devices are available. is there. Now, a silicon single crystal pulling apparatus will be described as a representative of them.

即ち石英ガラス(Ga-As系単結晶の場合には通常窒化ホウ
素)製ルツボにシリコン多結晶を充填する。この際使用
される石英ルツボは通常肉薄のものが使用されるためそ
の強度では石英が軟化したり、時に割れることもあるた
め、これの補強のために黒鉛ルツボに内挿する。そして
このシリコンを充填したルツボを回転させまたはそのま
まで高周波誘導加熱または抵抗式発熱体(ヒーター)に
より加熱し約1500℃前後に加熱してシリコンを溶融
する。ルツボ上部の引上機に支承されたシリコン単結晶
の種をシリコン溶融体中に浸漬し、これを引上げつつ徐
冷して他結晶体を単結晶体とするものである。
That is, a crucible made of quartz glass (usually boron nitride in the case of Ga-As series single crystal) is filled with silicon polycrystal. Since the quartz crucible used in this case is usually thin, its strength may cause the quartz to soften and sometimes break. Therefore, it is inserted into the graphite crucible to reinforce it. Then, the crucible filled with the silicon is rotated or heated as it is by a high frequency induction heating or a resistance type heating element (heater) and heated to about 1500 ° C. to melt the silicon. The seeds of the silicon single crystal supported by the pulling machine above the crucible are immersed in the silicon melt, which is then gradually cooled while being pulled to make another crystal into a single crystal.

この単結晶は主に半導体に使用されるために極めて高純
度であることが要求され、溶融体が直接接触する石英ガ
ラスは、その純度が非常に高いものが要求されるが、こ
れと共に用いられる装置内部の各部材についても高純度
のものが要求される。そしてこの引上装置に於いては、
上記した通り極めて高温であって耐熱性、低蒸気圧性が
要求され、現在そのほとんどは炭素材通常は黒鉛が使用
されている。
Since this single crystal is mainly used for semiconductors, it is required to have extremely high purity, and the quartz glass with which the melt directly contacts is required to have very high purity, but it is used together with this. Each member inside the apparatus is also required to have high purity. And in this lifting device,
As mentioned above, extremely high temperatures, heat resistance and low vapor pressure are required, and most of them are currently carbon materials, usually graphite.

しかし乍ら非常に高温のため炭素材中の不純物が滲出、
蒸散して、石英ルツボ内のシリコン溶融液を汚染し惹い
ては引上げ単結晶の品位を低下せしめ、結果として歩留
りを大きく低下せしめる。
However, due to the extremely high temperature, impurities in the carbon material leached out,
It evaporates and contaminates the silicon melt in the quartz crucible, which in turn lowers the quality of the pulled single crystal and, as a result, significantly lowers the yield.

しかも最近の技術の進歩により、高集積回路用基板とし
て益々超高純度の単結晶が要求されるようになり、これ
に伴い引上装置に使用する各黒鉛部材の高純度化が益々
要求されるようになって来た。
Moreover, due to recent technological advances, ultra-high-purity single crystals are increasingly required as substrates for highly integrated circuits, and along with this, high-purity graphite members used in pulling equipment are increasingly required. It came to be.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

本発明が解決しようとする問題点は、従来の単結晶引上
装置に要求される上記要望に応える装置を開発すること
であり、更に詳しくは極めて高純度であって、しかも単
結晶引上装置用部材として要求される各種特性、例えば
耐熱性、耐熱衝撃性、機械的特性、低蒸気圧性、化学的
安定性、低アウトガス性等を満足する黒鉛材料を開発
し、これを該装置の部材として使用することである。
The problem to be solved by the present invention is to develop an apparatus that meets the above-mentioned demands required for a conventional single crystal pulling apparatus, and more specifically, it is an extremely high purity single crystal pulling apparatus. We have developed a graphite material that satisfies the various characteristics required for materials such as heat resistance, thermal shock resistance, mechanical characteristics, low vapor pressure, chemical stability, and low outgassing. Is to use.

〔問題点を解決するための手段〕[Means for solving problems]

この問題点は全灰分が5ppm以下特に好ましくは1ppm以
下という極めて高純度の黒鉛材料を単結晶引上装置用の
部材として使用することによって解決される。
This problem is solved by using an extremely high purity graphite material having a total ash content of 5 ppm or less, particularly preferably 1 ppm or less, as a member for a single crystal pulling apparatus.

本発明者は従来から黒鉛材料就中高純度黒鉛材料につい
て研究を続けて来たが、この研究に於いて、従来の黒鉛
材料に比しその純度が極めて高く、しかも従来法の操作
上のトラブルを解決した黒鉛材料並びにその製法を開発
しすでに出願した(特願昭61−224131号)。更
に引き続く研究に於いて上記出願に係る新しい高純度黒
鉛材料が、単結晶引上装置の部材として極めて好適であ
って、この装置用部材として要求される諸特性を満足し
うるものであることを見出し、茲に本発明を完成するに
至ったものである。
The present inventor has been continuing research on graphite materials, especially high-purity graphite materials, and in this research, the purity thereof is extremely higher than that of conventional graphite materials, and further, the operational troubles of the conventional method are caused. A solved graphite material and a manufacturing method thereof have been developed and already filed (Japanese Patent Application No. 61-224131). In further subsequent research, it was confirmed that the new high-purity graphite material according to the above-mentioned application is extremely suitable as a member for a single crystal pulling apparatus and can satisfy various characteristics required as a member for this apparatus. The present invention has been completed based on the findings of headings.

〔発明の構成並びに作用〕[Structure and Action of Invention]

先ず本発明に於いて使用する高純度黒鉛材料について説
明する。
First, the high-purity graphite material used in the present invention will be described.

本発明の黒鉛材料は、その全灰分(不純分)が5ppm以
下特に好ましくは1ppm以下という極めて高純度のもの
であり、後記実施例からも明らかな通り、従来の黒鉛材
料或いは従来法による高純度化黒鉛材料に比しその純度
が極めて高い。尚、通常高純度化黒鉛材料として市販さ
れているものは全灰分が20〜50ppm程度のものであ
り、本発明の黒鉛材料は極めて高純度のものである。
The graphite material of the present invention has an extremely high purity such that the total ash content (impurity content) is 5 ppm or less, particularly preferably 1 ppm or less. As is apparent from the examples described below, the conventional graphite material or the high purity obtained by the conventional method is used. Its purity is extremely higher than that of chemical graphite materials. The commercially available high-purified graphite material generally has a total ash content of about 20 to 50 ppm, and the graphite material of the present invention is of extremely high purity.

この高純度黒鉛材料は次の様にして製造することが出来
る。即ち基本的には上記特願昭61−224231号の
方法によって製造される。更に詳しく説明すると以下の
通りである。
This high-purity graphite material can be manufactured as follows. That is, it is basically manufactured by the method of Japanese Patent Application No. 61-224231. A more detailed description is as follows.

炭素材を順次、焼成し、黒鉛化し、且つ高純度化する高
純度黒鉛材料の製造方法に於いて、高純度化を真空乃至
減圧下で高周波加熱手段により行う方法であり、更に好
ましい態様をあげれば以下の通りである。即ち (イ)炭素材を順次、焼成し、黒鉛化し次いで高純度化
する高純度黒鉛材の製造法に於いて、黒鉛化と高純度と
を同一装置で真空乃至減圧下に高周波加熱手段により行
うことを特徴とする製造方法、 (ロ)黒鉛化と高純度化とを一部重複して並行的に行う
製造方法、 (ハ)上記高純度黒鉛材の製造方法に於いて、黒鉛化及
び高純度化の少なくとも1つを100Torr乃至1Torrの
圧力下で高純度黒鉛材の製造方法、 (ニ)真空乃至減圧条件下に於ける高純度化工程に於い
て、ハロゲン化反応及びハロゲン化生成物の離脱反応を
同時に行わしめる製造方法、 等である。これ等方法について更に詳しく説明すると以
下の通りである。
A method for producing a high-purity graphite material in which a carbon material is sequentially fired, graphitized, and highly purified, is a method of performing high-purification by a high-frequency heating means under vacuum or reduced pressure, and a more preferable embodiment is exemplified. For example, That is, (a) in a method for producing a high-purity graphite material in which a carbon material is sequentially fired, graphitized, and then highly purified, graphitization and high purity are performed by a high-frequency heating means under vacuum or reduced pressure in the same apparatus. (B) a manufacturing method in which graphitization and high-purification are partially overlapped and performed in parallel, and (c) in the method for manufacturing a high-purity graphite material, At least one of the purification steps is a method for producing a high-purity graphite material under a pressure of 100 Torr to 1 Torr, and (d) a halogenation reaction and a halogenated product in a high-purification step under vacuum or reduced pressure conditions. A production method in which the withdrawal reaction is carried out simultaneously, and the like. The methods will be described in more detail below.

尚、説明の便宜上本製法の装置を示す図面を用いて本製
法を説明することとする。尚、第1図は本製法にかゝる
真空式・高周波加熱方式の高純度炭素材の製造装置の側
断面図を模式的に示したものである。
For convenience of explanation, the present manufacturing method will be described with reference to the drawings showing the apparatus of the present manufacturing method. Incidentally, FIG. 1 is a schematic side sectional view of a vacuum / high frequency heating type high-purity carbon material manufacturing apparatus according to the present manufacturing method.

本製法を構成する第一の要因は、原料素材の加熱に、床
面積が小さく、エネルギー効率の高い高周波加熱炉を採
用したことである。
The first factor that constitutes this manufacturing method is that a high-frequency heating furnace with a small floor area and high energy efficiency is used to heat the raw material.

第二の構成要因として誘導加熱炉の高周波コイル(105)
と被加熱炭素材(104)の中間に黒鉛ヒーター即ちサセプ
ター(106)を設けたことである。
The second component is the induction heating furnace high-frequency coil (105).
That is, a graphite heater, that is, a susceptor (106) is provided between the heated carbon material (104).

第三の構成要因として、上記の要因、即ち高周波コイル
(105)、サセプター(106)、被加熱炭素材(104)を減圧若
しくは真空に耐える密閉容器に収納することである。
The third factor is the above factor, that is, the high frequency coil.
(105), the susceptor (106), and the heated carbon material (104) are housed in a closed container that can withstand reduced pressure or vacuum.

尚、被加熱炭素材(104)、高周波コイル(105)、サセプタ
ー(106)を真空容器内に収納することは、本製法に於い
て下記に示すガス供給管(108)、ガス排出管(101)の設置
と共に最も重要な構成要因であり、これにより被加熱炭
素材(104)を効率よく、一貫して黒鉛化、高純度化を進
めることが可能になるものである。
The heating carbon material (104), the high frequency coil (105), and the susceptor (106) are housed in a vacuum container by the following gas supply pipe (108) and gas discharge pipe (101) in this manufacturing method. ) Is the most important constituent factor, and this makes it possible to efficiently and consistently graphitize and highly purify the heated carbon material (104).

第四の構成要因として該真空容器内に、ガス供給管(10
8)、ガス排出管(101)を設けることである。
As a fourth constituent factor, the gas supply pipe (10
8), the gas exhaust pipe (101) is provided.

ガス排出管(101)は容器内部を減圧又は真空にする際、
及び黒鉛化工程、高純度化工程に際し発生するガスの排
気に必要不可欠である。特に、高純度工程に於いて黒鉛
材から蒸散された金属ハロゲン化物、金属水素化化合物
等を反応系外に引き出す目的にも使用される。
The gas discharge pipe (101) is used when decompressing or vacuuming the inside of the container.
It is also indispensable for exhausting the gas generated during the graphitization process and the purification process. In particular, it is also used for the purpose of drawing out metal halides, metal hydride compounds, etc. evaporated from the graphite material out of the reaction system in the high purity step.

ガス供給管(108)は、高純度化工程に於いて使用される
ハロゲン含有ガス、又は/及びH2ガスを供給する目的
に使用される。
The gas supply pipe (108) is used for the purpose of supplying the halogen-containing gas used in the purification process and / or the H 2 gas.

これ等ガスの供給用と排出用の管は、真空容器の適宜の
場所に、必要に応じ複数個所に設けることが出来るが、
容器内のガスの流通と炭素材との接触効率を考えて、上
下、又は左右と対称側に設けることが望ましい。
These gas supply and discharge pipes can be provided at appropriate places in the vacuum container, and at a plurality of places as necessary.
Considering the flow of gas in the container and the efficiency of contact with the carbon material, it is desirable to provide them on the upper and lower sides or on the symmetrical side of the left and right sides.

第1図には縦型高周波炉を用い、ガス排出管(101)及び
供給管(108)を夫々上、下に設けた例を記したが、高周
波炉を横型にした場合には、これ等各管を夫々左、右に
設けることも出来る。
FIG. 1 shows an example in which a vertical high-frequency furnace is used and a gas discharge pipe (101) and a supply pipe (108) are provided above and below, respectively. Each tube can be installed on the left and right respectively.

以上の主要構成要因の他に、必要に応じて次の要因を付
加することが出来る。
In addition to the above main constituent factors, the following factors can be added as necessary.

即ち第五の要因として高周波コイルとサセプターの間に
断熱材(102)、(103)を用いることが出来る。断熱材とし
ては、セラミックファイバー、カーボンファイバー、カ
ーボンブラック等公知の材料を使用する。
That is, as the fifth factor, the heat insulating materials (102) and (103) can be used between the high frequency coil and the susceptor. As the heat insulating material, known materials such as ceramic fiber, carbon fiber and carbon black are used.

第六の要因として、必要により真空容器の外部に水冷ジ
ャケット(109)を設けることが出来る。
As a sixth factor, a water cooling jacket (109) can be provided outside the vacuum container if necessary.

高周波コイルには250〜3000Hzの高周波電圧が印
加され、真空容器の壁を貫いて内装されたコイルに電力
が供給される。
A high-frequency voltage of 250 to 3000 Hz is applied to the high-frequency coil, and power is supplied to the coil installed through the wall of the vacuum container.

次に上述の装置を用いた本製法の高純度黒鉛の製造方法
について記す。
Next, a method for producing high-purity graphite of the present production method using the above-mentioned apparatus will be described.

本製法は基本的には高純度化工程を真空乃至減圧下に高
周波加熱手段を用いて行う用法であり、その望ましい一
態様は上記第1図に示す本装置を用いて上記方法を行う
ものである。また本法に於いては、更に黒鉛化と高純度
化工程とを一つの炉で、これ等工程を順次、又は少なく
とも一部並行して行う方法も包含される。更に詳しく説
明すると以下の通りである。
This manufacturing method is basically a method of performing the high-purification step under vacuum or reduced pressure by using a high-frequency heating means, and one desirable mode thereof is to carry out the above-mentioned method using the present apparatus shown in FIG. is there. Further, the present method also includes a method in which the graphitization step and the high-purification step are performed in one furnace, and these steps are sequentially or at least partially performed in parallel. A more detailed description is as follows.

まずガス供給管(108)からN2ガスを送気して、容器内部
の空気をN2ガスで置換したのち、ガス排出管(101)から
減圧、又は真空に引き、雰囲気を非酸化性とする。
First, N 2 gas is sent from the gas supply pipe (108) to replace the air inside the container with N 2 gas, and then the gas exhaust pipe (101) is evacuated or evacuated to make the atmosphere non-oxidizing. To do.

次に誘導コイル(105)に徐々に電圧を印加してサセプタ
ー(106)を加熱し、その輻射熱により被加熱炭素材(104)
を800〜1000℃に通常1〜10時間好ましくは3
〜5時間保ったのち、徐々に昇温を続け、2450〜2
500℃に調節しながら5〜24時間好ましくは7〜1
5時間保持する。
Next, a voltage is gradually applied to the induction coil (105) to heat the susceptor (106), and the radiant heat of the heated carbon material (104).
To 800 to 1000 ° C. for usually 1 to 10 hours, preferably 3
After keeping it for ~ 5 hours, gradually raise the temperature to 2450 ~ 2
5 to 24 hours, preferably 7-1 while adjusting to 500 ° C
Hold for 5 hours.

容器内は加熱を始めた時点から1〜100Torrp好まし
くは10〜40Torr程度に保たれているので、この段階
で僅かに揮散してくる脱ガスの排出には好都合である。
Since the inside of the container is maintained at about 1 to 100 Torrp, preferably about 10 to 40 Torr from the time when heating is started, it is convenient to discharge the degassing gas that slightly volatilizes at this stage.

黒鉛化がある程度進んだ段階で、減圧状態のままガス供
給管(108)からハロゲンガス例えばジクロルジフルオル
メタンを(流量は容器内に充填する被加熱炭素材の量に
より増減されるが、例えば1〜7NTP/kg程度で3〜8
時間程度供給する。
At a stage where graphitization has progressed to a certain extent, a halogen gas such as dichlorodifluoromethane is supplied from the gas supply pipe (108) in a depressurized state (the flow rate is increased or decreased depending on the amount of the heated carbon material to be filled in the container. 3-8 at 1-7 NTP / kg
Supply about time.

高純度化に用いるハロゲンガスは、炭素材中に含まれる
不純物、特に金属不純物をハロゲン塩として蒸気圧を高
め、これの蒸発、揮散によって母材である炭素材の純度
を高めるために必要であるが、このハロゲンとしては従
来から使用されて来たものがいずれも使用出来、例えば
塩素や塩素化合物ばかりでなく弗素や弗素化合物も使用
出来、また更には塩素系或いは弗素系ガスを同時に併用
してもよい。また同一分子内に弗素と塩素とを含む化合
物、例えばモノクロロトリフルオルメタン、トリクロロ
モノフルオルメタン、ジクロルジフルオルエタン、トリ
クロロモノフルオルエタン等を使用することも出来る。
The halogen gas used for high purification is necessary to increase the vapor pressure by using impurities contained in the carbon material, particularly metal impurities, as a halogen salt to increase the vapor pressure, and evaporate and volatilize this to increase the purity of the carbon material that is the base material. However, as the halogen, any of those which have been conventionally used can be used. For example, not only chlorine and chlorine compounds but also fluorine and fluorine compounds can be used. Furthermore, chlorine or fluorine gas can be used together. Good. It is also possible to use a compound containing fluorine and chlorine in the same molecule, such as monochlorotrifluoromethane, trichloromonofluoromethane, dichlorodifluoroethane, trichloromonofluoroethane and the like.

また不純物の種類、例えは硫黄分等については、H2
高い精製効果を示すので、特に低硫黄グレード品につい
ては、ジクロルジフルオルメタンの供給を停止したの
ち、引き続いてH2ガスを供給することも出来る。
Regarding the type of impurities, for example, sulfur content, H 2 has a high refining effect, so especially for low sulfur grade products, after stopping the supply of dichlorodifluoromethane, continue to supply H 2 gas. You can also do it.

高純度化操作が完了した時点で、炉内の温度を更に上
げ、3000℃にて10〜30時間程度保って工程を完
了する。
When the high-purification operation is completed, the temperature in the furnace is further increased and the temperature is maintained at 3000 ° C. for about 10 to 30 hours to complete the process.

炉を冷却する工程の途中、約2000℃に於いて容器内
圧力を10-2乃至10-4Torrに強減圧し、冷却すること
により、アウトガスの少ない高純度炭素材を得ることが
出来る。
During the process of cooling the furnace, the pressure inside the vessel is strongly reduced to 10 -2 to 10 -4 Torr at about 2000 ° C, and the high-purity carbon material with less outgas can be obtained by cooling.

通電を停止、容器内にN2ガスを充填、置換し乍ら常
圧、常温に戻す。
Stop energizing, fill the container with N 2 gas, replace it, and return to normal pressure and room temperature.

上記方法は黒鉛化と高純度を一つの炉で行う方法を示し
ているが、本法に於いては高純度化だけを上記の方法で
行ってもよいことは勿論である。
Although the above method shows a method of performing graphitization and high purity in one furnace, it goes without saying that only high purity may be performed by the above method in this method.

本法により高純度化又はこれと黒鉛化を実施する際の容
器内の圧力は、100Torr乃至1Torrの範囲内に保つこ
とが望ましい。容器内の圧力は、ハロゲン化物、塩素化
又は/及び弗素化された不純物、又は置換時の残存N2
ガス等の種々の化合物の蒸気圧(分圧)の総和(全圧)
として圧力計に示されるが、これが100Torrより高い
場合は減圧効果が低くなり、従って高純度化に要する時
間は長くなり、品質的にも従来の常圧法と変りなく、ま
た1Torrに達しない場合ではハロゲン供給絶対量が少な
くなり、炭素材深部の高純度化が不充分になったり、ま
た生成ガスの排除に多大のポンプ動力を要し、得策では
ない。尚、100〜1Torr、特に好ましくは50〜5To
rrが最も良好な製品が得られる。
It is desirable to maintain the pressure in the container in the range of 100 Torr to 1 Torr when performing the purification or the graphitization with this method. The pressure in the container is set to be halide, chlorinated and / or fluorinated impurities, or residual N 2 upon substitution.
Sum of vapor pressure (partial pressure) of various compounds such as gas (total pressure)
If the pressure is higher than 100 Torr, the depressurizing effect will be low, and therefore the time required for high purification will be long, the quality will be the same as the conventional atmospheric pressure method, and if it does not reach 1 Torr. The absolute amount of halogen supply becomes small, the purification of deep carbon material becomes insufficient, and a large amount of pump power is required to remove the generated gas, which is not a good idea. Incidentally, 100 to 1 Torr, particularly preferably 50 to 5 Torr
The product with the best rr can be obtained.

本発明実施の一つの応用的態様として、高純度操作中、
反応容器内の圧力をパルス的に増減せしめる場合には、
炭素材の深層部へのハロゲンガスの拡散、置換及び深層
部からのハロゲン化生成物の離脱、置換が完全になり、
より効果的である。
As one applied aspect of the practice of the present invention, during high-purity operation,
To increase / decrease the pressure in the reaction vessel in a pulse,
Diffusion of halogen gas to the deep layer of carbon material, replacement, and elimination and replacement of halogenated products from the deep layer are complete,
More effective.

本発明の黒鉛材料としては、上記高純度の他に、更に等
方性であることが好ましい。この際の等方性とは、すべ
ての物的に於いて、各方向に於いてほぼ等しい性質を示
すことをいい、例えば電気的にも、熱体にもほぼ等しい
挙動を示すことを意味する。この等方性は本発明黒鉛材
を引上装置に使用する場合、その部材の種類、部位に応
じて電気抵抗、熱膨張率、機械的強度等要求される項目
に差異があるが、等方性炭素材は何れもこれ等を充足
し、特に本発明にかかる装置の構成材料としては異方比
が1.10以下特に1.03〜1.07以下の高度に等方化さ
れた材料が好ましい。この際の異方比とは、各材料の物
理的、機械的、電気的、化学的等の諸性質がx、y、z
各軸、各方向に対して最大値を最小値との比率が1.10
以下、好ましくは1.07〜1.03以下にあることを言
う。
In addition to the above-mentioned high purity, the graphite material of the present invention is preferably isotropic. In this case, the isotropic property means that all physical properties exhibit almost the same properties in each direction, and that, for example, they exhibit substantially the same behavior both electrically and in a heat body. . When the graphite material of the present invention is used in a pulling apparatus, this isotropy is different in required items such as electrical resistance, coefficient of thermal expansion, and mechanical strength depending on the type and site of the member. All of the carbonaceous materials satisfy these requirements, and particularly as a constituent material of the device according to the present invention, a highly isotropic material having an anisotropic ratio of 1.10 or less, particularly 1.03 to 1.07 or less. preferable. In this case, the anisotropic ratio means that physical, mechanical, electrical and chemical properties of each material are x, y and z.
The ratio of the maximum value to the minimum value is 1.10 for each axis and each direction.
Hereinafter, it is preferably 1.07 to 1.03 or less.

以下に本発明の引上装置について第2図を用いて説明す
る。ただし第2図は本発明装置の一部を示す図面であ
り、説明の便宜上これを模擬的に(イ)〜(ニ)の4図
に別けて表したものである。第2図(イ)は主にルツボ
を中心とした部分を、同図(ロ)は主に側部を中心とし
た部分を、同図(ハ)はルツボの下部を中心とした部分
を、また同図(ニ)は上部並びに下部を中心とした部分
を示す模擬的な断面説明図を示す。同図中(1)は黒鉛
ルツボ、(2)は黒鉛ヒーター、(3)は保温筒、
(4)は断熱材、(5)は緩衝材、(6)はスペーサ
ー、(7)はルツボ受皿、(8)はルツボ受更の支持
体、(9)はルツボ受皿の維持体カバー、(10)は電極
(ヒーター)とクランプとを固定するための固締具、
(11)は蒸気洩れ防止リング、(12)は電極(ヒータ
ー)、(13)は電極用クランプ、(14)は液漏れ用受
皿、(15)は上部蓋を示す。また(16)は石英または窒
化ホウ素製ルツボ、(17)はシリコンを示す。
The pulling apparatus of the present invention will be described below with reference to FIG. However, FIG. 2 is a drawing showing a part of the device of the present invention, and for convenience of explanation, this is schematically shown separately in FIG. 4 of (a) to (d). Fig. 2 (a) mainly shows the part centering on the crucible, Fig. 2 (b) mainly shows the part centering on the side, and Fig. 2 (c) shows the part centering on the lower part of the crucible, Further, FIG. 4D is a schematic cross-sectional explanatory view showing a portion centering on the upper portion and the lower portion. In the figure, (1) is a graphite crucible, (2) is a graphite heater, (3) is a heat insulating tube,
(4) is a heat insulating material, (5) is a cushioning material, (6) is a spacer, (7) is a crucible tray, (8) is a support for crucible replacement, and (9) is a crucible tray retainer cover, ( 10) is a fastener for fixing the electrode (heater) and the clamp,
(11) is a vapor leakage prevention ring, (12) is an electrode (heater), (13) is an electrode clamp, (14) is a liquid leakage tray, and (15) is an upper lid. Further, (16) indicates a crucible made of quartz or boron nitride, and (17) indicates silicon.

本発明の装置は上記(1)〜(15)の各部材の少なくと
も1種が上記高純度黒鉛材料から成るものであり、好ま
しくは(1)〜(3)の 各部材が共に上記高純度黒鉛
材料から成るものである。
In the apparatus of the present invention, at least one of the members (1) to (15) is made of the high purity graphite material, and preferably, the members (1) to (3) are both the high purity graphite. It consists of materials.

黒鉛ルツボ(1)はその内部の石英または窒化ホウ素製
ルツボを保護補強するために使用されるものであり、そ
の形状、大きさ等は従来のものと特に変わらない。ヒー
ター(2)はこの第2図では抵抗式の場合を示してい
る。また保温筒(3)はヒーター(2)からの輻射熱を
反射するためと、断熱材(4)の保護のために使用され
るもので、厚みは通常3〜12好ましくは5〜8mm程度
である。通常この保温筒(3)は黒鉛ルツボ(2)との
間に若干空間を設け、また断熱材(4)とは空間を設け
または設けずに設置される。これ等(1)〜(3)の部
材は高純度であると共に等方姓であることが特に好まし
い。等方性であることにより、耐破損性が向上し、加工
が容易となり、熱膨張が等方的となり、特にヒーター
(2)では電気特性が均一となる。断熱材(4)は断熱
のために使用され、ヒーター(2)と外壁との間に設け
られ断熱、保温効果を発揮する。
The graphite crucible (1) is used to protect and reinforce the quartz or boron nitride crucible inside, and its shape and size are not particularly different from those of the conventional one. The heater (2) is of a resistance type in FIG. The heat insulating tube (3) is used for reflecting the radiant heat from the heater (2) and for protecting the heat insulating material (4), and the thickness thereof is usually 3 to 12 and preferably about 5 to 8 mm. . Usually, the heat insulating tube (3) is provided with a slight space between it and the graphite crucible (2), and is installed with or without a space with the heat insulating material (4). It is particularly preferable that these members (1) to (3) have high purity and areotropic. By being isotropic, damage resistance is improved, processing is facilitated, and thermal expansion is isotropic, and particularly the heater (2) has uniform electric characteristics. The heat insulating material (4) is used for heat insulation and is provided between the heater (2) and the outer wall to exhibit heat insulating and heat retaining effects.

断熱材(4)は断熱のために使用され、ヒーター(2)
と外壁との間に設けられ、断熱、保温効果を発揮する。
Insulation (4) is used for insulation, heater (2)
It is installed between the outer wall and the outer wall, and exerts heat insulation and heat retention effects.

本発明装置に於いて緩衝材(5)は石英ルツボ(16)と
黒鉛ルツボ(1)との間にあって、これ等の間で緩衝作
用を発揮し、両ルツボの保護のために使用される。また
ルツボの位置(高さ)を調整する作用をも有する。この
緩衝材(5)としては波形シートや平面シートが使用さ
れる。これ等断熱材並びに緩衝材は必ずしも等方性でな
くても良く、黒鉛フェルト、発泡黒鉛圧密体、中空バル
ーン黒鉛球、またはその圧密体、及び黒鉛材を黒鉛質外
被材で被覆したものでも良い。スペーサー(6)は黒鉛
ルツボ(1)とルツボ受皿(7)との間にあってこれ等
の断熱作用、位置調節及び緩衝材として使用される。使
用される材料としては黒鉛黒鉛圧密体、中空黒鉛球を樹
脂またはピッチで固めて炭化したもの等、及びそれ等と
平板状等方性炭素材との積層構造体が用いられるが、何
れの材料も全灰分が5ppm以下であることが必要であ
る。ルツボ受皿はルツボを所定の位置にセットするため
に使用され、等方性黒鉛材を使用することが好ましい。
またこの際炭素繊維で補強した黒鉛材(以下複合材とい
う)を使用しても良い。
In the device of the present invention, the cushioning material (5) is located between the quartz crucible (16) and the graphite crucible (1), exerts a cushioning action between them, and is used to protect both crucibles. It also has the function of adjusting the position (height) of the crucible. A corrugated sheet or a flat sheet is used as the cushioning material (5). These heat insulating materials and cushioning materials do not necessarily have to be isotropic, and graphite felt, expanded graphite compacts, hollow balloon graphite spheres or compacts thereof, and graphite materials coated with a graphite jacket material good. The spacer (6) is located between the graphite crucible (1) and the crucible tray (7) and is used as a heat insulating function, a position adjusting member, and a cushioning member. As the material used, a graphite graphite compact, a hollow graphite sphere solidified with resin or pitch and carbonized, and a laminated structure of these and a flat plate-like isotropic carbon material are used. It is also necessary that the total ash content be 5 ppm or less. The crucible tray is used to set the crucible at a predetermined position, and isotropic graphite material is preferably used.
At this time, a graphite material reinforced with carbon fibers (hereinafter referred to as a composite material) may be used.

ルツボ受皿の支持体(8)は、ルツボ受皿(7)の支持
のために使用され、ルツボ受皿と別々に、またはこれと
一体的になしても良い。この支持体(8)とても黒鉛材
料として複合材を使用しても良く、また等方性のものを
使用するのが好ましい。
The crucible pan support (8) is used for supporting the crucible pan (7) and may be separate from or integral with the crucible pan. The support (8) may be a composite material as the graphite material, and isotropic material is preferably used.

カバー(9)は支持体(8)をシリコン蒸気から保護す
る目的で使用され、やはり等方性であることが好まし
く、また複合材を用いても良い。
The cover (9) is used for the purpose of protecting the support (8) from silicon vapor, is preferably isotropic as well, and a composite material may be used.

また固締具(10)としては、電極(ヒーター)とクラン
プ(13)とを固締するために使用されるため複合材を使
用することが好ましい。
As the fastening tool (10), a composite material is preferably used because it is used to fasten the electrode (heater) and the clamp (13).

蒸気洩れ防止リング(11)は必ずしも必要ではないが、
ルツボ内の蒸気が上部に移動するのを防ぐ作用を有し、
黒鉛材としては等方性であることが好ましい。
The vapor leak prevention ring (11) is not always necessary,
Has a function to prevent the vapor in the crucible from moving to the upper part,
The graphite material is preferably isotropic.

本発明装置は、上記各部材の少なくとも1種が超高純度
黒鉛材からなっており、また好ましくは等方性のものま
たは複合材から成っているために、結果として高純度の
単結晶が収得出来るものである。
In the device of the present invention, at least one of the above members is made of an ultra-high purity graphite material, and preferably isotropic or a composite material, and as a result, a high-purity single crystal can be obtained. It can be done.

いま、本発明の黒鉛材が超高純度であることを示すため
に、第1表に本発明にかゝる装置及び方法により製造せ
られたる超高純度黒鉛材中の不純物量と、従来法により
得られたる市販高純度品中の不純物量、並びに高純度処
理を全く行わない通常の黒鉛材の不純物量を対比して示
した。
In order to show that the graphite material of the present invention has an ultrahigh purity, Table 1 shows the amount of impurities in the ultrahigh purity graphite material produced by the apparatus and method according to the present invention and the conventional method. The amount of impurities in the commercially available high-purity product obtained in step 1 and the amount of impurities in the ordinary graphite material not subjected to the high-purity treatment are shown in comparison.

但し上記A、B及びCの各試料は夫々次のものである。 However, the samples A, B, and C are as follows.

試料A:本発明法による製品。原料黒鉛材は試料Cを高
純度化容器を用いて内圧20〜25Torr、900℃で4
HR、2450〜2500℃で10HR、途中ゾクロルジフ
ルオルメタン3NTR/kgで高純度化、更に3000℃に
て20HRの条件で製造したもの。
Sample A: Product according to the method of the invention. As the raw graphite material, sample C was used in a high-purification container at an internal pressure of 20 to 25 Torr and at 900 ° C. for 4 hours.
HR, manufactured at 2450 to 2500 ° C for 10 HR, zochlorodifluoromethane 3NTR / kg for high purification, and 3000 ℃ for 20 HR.

試料B:試料Cを公知方法による常圧高純度化処理を行
ったもの。
Sample B: Sample C that has been subjected to atmospheric pressure high-purification treatment by a known method.

試料C:市販品(見掛け密度1.80の等方性黒鉛材、高
純度化する前のもの)、東洋炭素(株)製。
Sample C: Commercial product (isotropic graphite material with apparent density of 1.80, before purification), manufactured by Toyo Tanso Co., Ltd.

また分析方法は発光分光分析法及び原子吸光分析によっ
た。数字の単位はppm、(−)印は「検出されず」を表
す。
The analysis method was based on emission spectroscopy and atomic absorption spectrometry. The unit of the number is ppm, and the (-) mark represents "not detected".

尚、本発明の何れの材料に於いても、全灰分が5ppm以
下であることが必要である。
It should be noted that in any of the materials of the present invention, it is necessary that the total ash content is 5 ppm or less.

因に、前記試料A、B及びCの全灰分量は、日本工業規
格(JIS)R7223−1979に準拠して測定し
て、夫々1ppm、10ppm、410ppmであり、従って試
料Aは本発明範囲内、試料B及びCは本発明範囲外であ
る。
Incidentally, the total ash content of the samples A, B, and C was 1 ppm, 10 ppm, and 410 ppm, respectively, measured according to Japanese Industrial Standard (JIS) R7223-1979, and therefore the sample A is within the scope of the present invention. , Samples B and C are outside the scope of the invention.

前記第1表に於ける分析値に示す如く、本発明装置に適
用される黒鉛材としては、高純度化反応装置から取り出
された状態での全灰分量としては1ppm以下、実質的に
0ppm(検出されない程度)に近いものであるが、取り
出されたあと、包装、運送、引上げ装置内に装着する作
業工程等において、取扱い中、若干の汚染は避けられ
ず、このため少なくとも5ppmの高純度化炭素材を使用
するものである。
As shown in the analysis values in Table 1, the graphite material applied to the apparatus of the present invention has a total ash content of 1 ppm or less, substantially 0 ppm ( Although it is almost undetectable), some contamination is unavoidable during handling in the work process such as packaging, transportation, and installation in the pulling device after it is taken out. A carbon material is used.

尚、本発明においては、全灰分5ppm以下の高純度黒鉛
材料を用いることにより、前述した様に、引上単結晶の
品質に影響を与える黒鉛部材のアウトガス性等の性質が
改良されるという効果がある。この点をより明瞭になす
見地より、前記試料A、B及びCのアウトガス性を測定
した。
In the present invention, the use of a high-purity graphite material having a total ash content of 5 ppm or less improves the properties of the graphite member such as the outgassing property, which affects the quality of the pulled single crystal, as described above. There is. From the viewpoint of making this point clearer, the outgassing properties of the samples A, B and C were measured.

測定方法は、石英管内に試料(寸法10×10×10m
m)を入れ、真空ポンプで排気し、石英管のコックを閉
めて試料を20分間加熱した。コックを用いて発生した
ガスを質量分析計に導入して、圧力測定及び定性・定量
分析を行った。結果を第3図に示す。
The measuring method is as follows.
m) was put in, the gas was evacuated by a vacuum pump, the cock of the quartz tube was closed, and the sample was heated for 20 minutes. The gas generated using a cock was introduced into a mass spectrometer, and pressure measurement and qualitative / quantitative analysis were performed. Results are shown in FIG.

全灰分が1ppmの試料Aのアウトガス性は全灰分10ppm
(試料B)と410ppm(試料C)のものと特性が異な
っており、特に約900℃から1100℃の温度範囲に
おいて、試料Aはアウトガス量にほとんど変化はなく平
坦化を示しているが、試料B(全灰分10ppm)と試料
C(全灰分410ppm)は、アウトガス量の増加が見ら
れ、温度1100℃における試料Bと試料Cのアウトガ
ス量は、Aと比較すると、夫々約3.8倍と約13倍多
くなっている。
Outgassing of Sample A with a total ash content of 1 ppm is 10 ppm total ash content
The characteristics are different from those of (Sample B) and 410 ppm (Sample C), and especially in the temperature range of about 900 ° C to 1100 ° C, Sample A shows almost no change in the outgas amount and shows flattening. B (total ash content 10 ppm) and sample C (total ash content 410 ppm) showed an increase in outgas amount, and the outgas amount of sample B and sample C at a temperature of 1100 ° C were about 3.8 times that of A, respectively. About 13 times more.

又全灰分5ppmのものも同様にアウトガス性を調べたと
ころ、全灰分1ppmの試料Aの特性と余り変わらず、全
灰分1ppmで見られた約900℃〜1100℃間の平坦
化は全灰分5ppmのものでも見られた。
Similarly, when the outgassing property of the total ash content of 5 ppm was also examined, it was not much different from the characteristics of the sample A having the total ash content of 1 ppm, and the flattening between about 900 ° C. and 1100 ° C. observed at the total ash content of 1 ppm was 5 ppm total ash content. Also seen in the one.

試料Aで見られた約900℃〜1100℃間のアウトガ
ス量の平坦化は、全灰分が5ppmを越えるとこの平坦化
を示さなくなり、アウトガス量は多くなり始めるため、
このガスが拡散されて溶融体中に取り込まれ、単結晶中
の純度に影響を与える。実際に全灰部が5ppm以下の黒
鉛材と5ppmを越えるもので比較すると、シリコン単結
晶引上を行ったところ、単結晶の品位確保や結晶欠陥発
生防においてその結果に顕著な差があることがわかっ
た。
The flattening of the outgas amount between about 900 ° C. and 1100 ° C. observed in Sample A does not show this flattening when the total ash content exceeds 5 ppm, and the outgas amount starts to increase.
This gas is diffused and taken into the melt, which affects the purity in the single crystal. Compared with a graphite material whose total ash content is 5 ppm or less and a material whose total ash content exceeds 5 ppm, a silicon single crystal pull-up shows that there are significant differences in the results in terms of ensuring the quality of the single crystal and preventing crystal defects. I understood.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明に於いて使用する高純度黒鉛材の製造装
置の一例の断面図を模擬的に示したものであり、第2図
は本発明装置の一例を模擬的に表わしたものである。第
3図は、本発明範囲内のA試料(全灰分1ppm)、本発
明範囲外の試料B及びC(10ppm及び410ppm)のア
ウトガス性の測定結果を示した曲線図である。 (1)……黒鉛ルツボ (2)……黒鉛ヒーター (3)……保温筒 (4)……断熱材 (5)……緩衝材 (6)……スペーサー (7)……ルツボ受皿 (8)……ルツボ受皿の支持体 (9)……ルツボ受皿の支持体カバー (10)……電極(ヒーター)とクランプを固定するため
の固締具 (11)……蒸気洩れ防止リング (12)……電極ヒーター (13)……電極ヒーター用クランプ (14)……液漏れ用受皿 (15)……上部蓋 (16)……石英または窒化ホウ素製ルツボ (17)……シリコン (101)……ガス排出管 (102)……保温材 (103)……保温材 (104)……被加熱炭素材 (105)……高周波コイル (106)……サセプター (107)……受皿 (108)……ガス供給管 (109)……ジャケット (301)……全灰分1ppm)のアウトガス曲線 (302)……全灰分10ppm)のアウトガス曲線 (303)……全灰分410ppm)のアウトガス曲線
FIG. 1 is a schematic sectional view of an example of an apparatus for producing a high-purity graphite material used in the present invention, and FIG. 2 is a schematic view of an example of the apparatus of the present invention. is there. FIG. 3 is a curve diagram showing the results of measuring the outgassing properties of sample A (total ash content 1 ppm) within the scope of the present invention and samples B and C (10 ppm and 410 ppm) outside the scope of the present invention. (1) …… Graphite crucible (2) …… Graphite heater (3) …… Insulation cylinder (4) …… Insulation material (5) …… Buffer material (6) …… Spacer (7) …… Crucible saucer (8) ) …… Support for crucible saucer (9) …… Support for crucible saucer (10) …… Fastener for fixing electrode (heater) and clamp (11) …… Steam leakage prevention ring (12) Electrode heater (13) Electrode heater clamp (14) Liquid leakage saucer (15) Top lid (16) …… Quartz or boron nitride crucible (17) …… Silicone (101)… … Gas exhaust pipe (102)… Heat insulation material (103)… Heat insulation material (104)… Carbon material to be heated (105)… High frequency coil (106)… Susceptor (107)… Saucepan (108)… … Gas supply pipe (109) …… Jacket (301) …… Outgas curve of total ash content 1ppm) (302) …… Total ash content 10 ppm) outgas curve (303) ... total ash content 410ppm) outgas curve

Claims (15)

【特許請求の範囲】[Claims] 【請求項1】単結晶引上装置に於いて、黒鉛ルツボ、黒
鉛ヒーター及び黒鉛保温筒の少なくとも1種が、全灰分
5ppm以下の高純度黒鉛材料から成ることを特徴とする
単結晶引上装置。
1. A single crystal pulling apparatus, wherein at least one of a graphite crucible, a graphite heater and a graphite heat insulating tube is made of a high purity graphite material having a total ash content of 5 ppm or less. .
【請求項2】黒鉛ヒーターと反応室外壁との間に使用さ
れる断熱材を構成する材料の少なくとも一部が全灰分5
ppm以下の高純度黒鉛材料から成ることを特徴とする特
許請求の範囲第1項に記載の単結晶引上装置。
2. A total ash content of at least a part of the material constituting the heat insulating material used between the graphite heater and the outer wall of the reaction chamber is 5.
The single crystal pulling apparatus according to claim 1, which is made of a high-purity graphite material of ppm or less.
【請求項3】内部ルツボと黒鉛ルツボとの間に使用され
る緩衝材が全灰分5ppm以下の高純度黒鉛材料である特
許請求の範囲第1項に記載の単結晶引上装置。
3. The single crystal pulling apparatus according to claim 1, wherein the cushioning material used between the inner crucible and the graphite crucible is a high-purity graphite material having a total ash content of 5 ppm or less.
【請求項4】黒鉛ルツボと黒鉛ルツボ受皿との間に使用
されるスペーサーが全灰分5ppm以下の高純度黒鉛材料
である特許請求の範囲第1項に記載の単結晶引上装置。
4. The single crystal pulling apparatus according to claim 1, wherein the spacer used between the graphite crucible and the graphite crucible tray is a high-purity graphite material having a total ash content of 5 ppm or less.
【請求項5】黒鉛ルツボの直下に位置する黒鉛ルツボ受
皿が全灰分5ppm以下の高純度黒鉛材料から成ることを
特徴とする特許請求の範囲第1項に記載の単結晶引上装
置。
5. The apparatus for pulling a single crystal according to claim 1, wherein the graphite crucible tray located immediately below the graphite crucible is made of a high-purity graphite material having a total ash content of 5 ppm or less.
【請求項6】ルツボ受皿の支持体が全灰分5ppm以下の
高純度黒鉛材料である特許請求の範囲第1項に記載の単
結晶引上装置。
6. The single crystal pulling apparatus according to claim 1, wherein the support of the crucible tray is a high-purity graphite material having a total ash content of 5 ppm or less.
【請求項7】ルツボ受皿の支持体カバーが全灰分5ppm
以下の高純度黒鉛材料から成ることを特徴とする特許請
求の範囲第1項に記載の単結晶引上装置。
7. The support cover of the crucible tray has a total ash content of 5 ppm.
The single crystal pulling apparatus according to claim 1, which is made of the following high-purity graphite material.
【請求項8】ルツボ受皿の下部に位置する液洩れ用受皿
が全灰分5ppm以下の高純度黒鉛材料である特許請求の
範囲第1項に記載の単結晶引上装置。
8. The apparatus for pulling a single crystal according to claim 1, wherein the liquid-leaking tray located under the crucible tray is a high-purity graphite material having a total ash content of 5 ppm or less.
【請求項9】電極用クランプ(連結棒)が全灰分5ppm
以下の高純度黒鉛材料から成ることを特徴とする特許請
求の範囲第1項に記載の単結晶引上装置。
9. The total ash content of the electrode clamp (connecting rod) is 5 ppm.
The single crystal pulling apparatus according to claim 1, which is made of the following high-purity graphite material.
【請求項10】電極とクランプとを固締するための固締
具が全灰分5ppm以下の高純度黒鉛材料から成ることを
特徴とする特許請求の範囲第1項に記載の単結晶引上装
置。
10. The apparatus for pulling a single crystal according to claim 1, wherein the fastening tool for fastening the electrode and the clamp is made of a high-purity graphite material having a total ash content of 5 ppm or less. .
【請求項11】蒸気洩れ防止リングが全灰分5ppm以下
の高純度黒鉛材料から成ることを特徴とする特許請求の
範囲第1項に記載の単結晶引上装置。
11. The single crystal pulling apparatus according to claim 1, wherein the vapor leakage prevention ring is made of a high-purity graphite material having a total ash content of 5 ppm or less.
【請求項12】上記単結晶が半導体用単結晶である特許
請求の範囲第1乃至11項のいずれかに記載の単結晶引
上装置。
12. The single crystal pulling apparatus according to claim 1, wherein the single crystal is a semiconductor single crystal.
【請求項13】上記高純度黒鉛材料が等方性である特許
請求の範囲第1乃至11項のいずれかに記載の単結晶引
上装置。
13. A single crystal pulling apparatus according to any one of claims 1 to 11, wherein the high-purity graphite material is isotropic.
【請求項14】上記等方性の範囲が異方比1.1以下であ
る特許請求の範囲第1乃至11項のいずれかに記載の単
結晶引上装置。
14. The apparatus for pulling a single crystal according to claim 1, wherein the isotropic range is an anisotropic ratio of 1.1 or less.
【請求項15】上記異方比が1.03〜1.10の範囲であ
る特許請求の範囲第1乃至11項のいずれかに記載の単
結晶引上装置。
15. The single crystal pulling apparatus according to any one of claims 1 to 11, wherein the anisotropic ratio is in the range of 1.03 to 1.10.
JP62174398A 1987-07-13 1987-07-13 Single crystal pulling device Expired - Lifetime JPH062637B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62174398A JPH062637B2 (en) 1987-07-13 1987-07-13 Single crystal pulling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62174398A JPH062637B2 (en) 1987-07-13 1987-07-13 Single crystal pulling device

Publications (2)

Publication Number Publication Date
JPS6418986A JPS6418986A (en) 1989-01-23
JPH062637B2 true JPH062637B2 (en) 1994-01-12

Family

ID=15977884

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62174398A Expired - Lifetime JPH062637B2 (en) 1987-07-13 1987-07-13 Single crystal pulling device

Country Status (1)

Country Link
JP (1) JPH062637B2 (en)

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US8097331B2 (en) 2006-07-31 2012-01-17 Toyo Tanso Co., Ltd. Mold release sheet
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