JPH0218376A - Granular silicon raw material supply device - Google Patents
Granular silicon raw material supply deviceInfo
- Publication number
- JPH0218376A JPH0218376A JP16508488A JP16508488A JPH0218376A JP H0218376 A JPH0218376 A JP H0218376A JP 16508488 A JP16508488 A JP 16508488A JP 16508488 A JP16508488 A JP 16508488A JP H0218376 A JPH0218376 A JP H0218376A
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- silicon
- single crystal
- guide tube
- granular silicon
- 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.)
- Pending
Links
Landscapes
- Crystals, And After-Treatments Of Crystals (AREA)
- Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、シリコン単結晶を引上げながら粒状シリコン
原料を供給するチョクラルスキー法によるシリコン単結
晶の製造装置において、上記粒状シリコン原料をるつぼ
に供給するための原料供給装置に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a silicon single crystal manufacturing apparatus using the Czochralski method in which a granular silicon raw material is supplied while pulling a silicon single crystal, in which the granular silicon raw material is placed in a crucible. The present invention relates to a raw material supply device for supplying raw materials.
[従来の技術]
シリコン単結晶(以下単に単結晶ということがある)の
製造には、るつぼ内に保持されたシリコン融液から、種
結晶を用いて単結晶を引上げる、いわゆるチョクラルス
キー法(CZ法)が広〈実施されている。[Prior art] Silicon single crystals (hereinafter sometimes simply referred to as single crystals) are manufactured using the so-called Czochralski method, in which a single crystal is pulled from a silicon melt held in a crucible using a seed crystal. (CZ Law) is widely implemented.
この方法では、シリコン単結晶の抵抗率の制御の目的で
、p型半導体用としてボロン、N型半導体用としてリン
、アンチモンなどをシリコン融液中にあらかじめ添加し
ている。しかし、これらの添加元素は、シリコン融液が
単結晶に凝固する際に一定の割合で単結晶中にとりこま
れ、残りは残シリコン融液中に排出される。そして、単
結晶引上げにともなうシリコン融液の減少により、シリ
コン融液中のドープ剤濃度が増加し、このため引上げら
れる単結晶中のドープ剤濃度も、単結晶の頭部から尾部
にかけて次第に増加する。従って低効率も変化し、単結
晶からシリコンウェハを製造したときはウェハごとに電
気電動率が異なることになり、要求が厳しい場合には、
使用可能なウェハの歩留りが50%以下になることもあ
る。In this method, for the purpose of controlling the resistivity of the silicon single crystal, boron for a p-type semiconductor, phosphorus, antimony, etc. for an n-type semiconductor are added to the silicon melt in advance. However, when the silicon melt solidifies into a single crystal, these additive elements are incorporated into the single crystal at a constant rate, and the rest is discharged into the remaining silicon melt. As the silicon melt decreases as the single crystal is pulled, the dopant concentration in the silicon melt increases, and therefore the dopant concentration in the pulled single crystal gradually increases from the head to the tail of the single crystal. . Therefore, the low efficiency also changes, and when silicon wafers are manufactured from single crystals, the electrical efficiency varies from wafer to wafer, and if the requirements are strict,
The yield of usable wafers may be less than 50%.
このようなことから、シリコン単結晶の引上げ量に見合
ったシリコン原料をるつぼ内のシリコン融液に投入して
融解させ、シリコン融液の液面及びドープ剤濃度を常に
一定に保持する方法が提案されている。For this reason, a method has been proposed in which a silicon raw material corresponding to the amount of silicon single crystal pulled is poured into the silicon melt in a crucible and melted, and the liquid level and dopant concentration of the silicon melt are always kept constant. has been done.
この方法は、加熱炉の外部に設けた原料供給装置に、加
熱炉内に設けられた案内管の一端を接続してシリコン融
液に粒状シリコン原料を供給するようにしたものである
。しかしながらこのような方法においては、投下された
粒状シリコン原料によってシリコン融液に波立ちが発生
する、投下された粒状シリコン原料が完全に溶解する前
に中央部で育成されたシリコン単結晶に付着する等の理
由により、成長中のシリコン単結晶が有転位化するとい
う問題が生じる。In this method, one end of a guide tube provided inside the heating furnace is connected to a material supply device provided outside the heating furnace to supply granular silicon raw material to the silicon melt. However, in this method, the dropped granular silicon raw material causes ripples in the silicon melt, or the dropped granular silicon raw material adheres to the silicon single crystal grown in the center before it is completely melted. For this reason, a problem arises in that the growing silicon single crystal becomes dislocated.
そこで、このような問題を防止するため、るつぼ内にこ
れと同心的でかつ下部に連通部を有するリング状の仕切
りを設け、仕切りの内側に単結晶育成部を、また仕切り
の外側に原料供給部を形成し、この原料供給部に粒状シ
リコン原料を供給する方法が提案される。例えば、実開
昭59−141578号公報に開示された考案は、粒状
シリコン原料を投入する案内管の開口部を、原料供給部
のシリコン融液の液面からなり上方に位置させたもので
あり、また特開昭58−130195号公報に開示され
た発明は、案内管の先端部を原料供給部のシリコン融液
中に挿入したものである。Therefore, in order to prevent such problems, a ring-shaped partition that is concentric with the crucible and has a communication section at the bottom is installed inside the crucible, and the single crystal growth section is placed inside the partition, and the raw material is supplied outside the partition. A method is proposed in which a part is formed and a granular silicon raw material is supplied to this raw material supply part. For example, in the device disclosed in Japanese Utility Model Application Publication No. 59-141578, the opening of the guide tube into which the granular silicon raw material is introduced is located above the liquid level of the silicon melt in the raw material supply section. In the invention disclosed in Japanese Patent Application Laid-Open No. 58-130195, the tip of the guide tube is inserted into the silicon melt in the raw material supply section.
[発明が解決しようとする課題]
実開昭59−141578号公報に開示された考案にお
いては、落下中の粒状シリコン原料のぶつかり合いや、
融液液面でのはね返り等によって多量の粒状シリコン原
料が単結晶育成部に入り込み、成長中のシリコン単結晶
が有転位化するという問題があり、このため継続的にシ
リコン単結晶の育成を行なうことができないという問題
がある。[Problems to be Solved by the Invention] In the invention disclosed in Japanese Utility Model Application Publication No. 59-141578, the collision of falling granular silicon raw materials,
There is a problem in that a large amount of granular silicon raw material enters the single crystal growth zone due to splashing on the melt surface, and the growing silicon single crystal becomes dislocated. Therefore, silicon single crystals are grown continuously. The problem is that I can't.
また特開昭58−13095号公報に開示された発明は
、粒状シリコン原料を投入した際、るつぼ内の熱環境か
ら案内管内でシリコン融液が凝固する可能性が大であり
、この方法は実施困難である。Furthermore, in the invention disclosed in JP-A No. 58-13095, when the granular silicon raw material is introduced, there is a high possibility that the silicon melt will solidify in the guide tube due to the thermal environment in the crucible, so this method is not practical. Have difficulty.
本発明は、上記の課題を解決するためになされたもので
、原料供給部に投入された粒状シリコン原料が単結晶育
成部に侵入するおそれがなく、したがって、育成された
シリコン単結晶が有転位化することのない粒状シリコン
原料の供給装置を得ることを目的としたものである。The present invention has been made to solve the above problems, and there is no fear that the granular silicon raw material fed into the raw material supply section will enter the single crystal growth section, so that the grown silicon single crystal will have dislocations. The object of the present invention is to obtain a supply device for a granular silicon raw material that does not become oxidized.
[課題を解決するための手段〕
本発明は、上記の目的を達成するためになされたもので
、リング状の仕切りを有するるつぼを備え、前記仕切り
の内側からシリコン単結晶を引上げると共に、前記仕切
りの外側に案内管により粒状シリコン原料を連続的に供
給してシリコン単結晶を製造する装置において、前記案
内管の先端部に該案内管の外径より大きい遮蔽部を設け
、該遮蔽部を前記るつぼの仕切りの外側のシリコン融液
の液面に近接し又はその一部を浸漬して配置した粒状シ
リコン原料の供給装置。及び、
上記装置において、前記案内管の途中に、前記粒状シリ
コン原料の落下速度減速部を設けた粒状シリコン原料の
供給装置を提供するものである。[Means for Solving the Problems] The present invention has been made to achieve the above object, and includes a crucible having a ring-shaped partition, pulling a silicon single crystal from inside the partition, and pulling the silicon single crystal from the inside of the partition. In an apparatus for manufacturing silicon single crystals by continuously supplying granular silicon raw material to the outside of a partition through a guide tube, a shielding portion larger than the outer diameter of the guide tube is provided at the tip of the guide tube, and the shielding portion is A supply device for granular silicon raw material, which is disposed close to or partially immersed in the surface of the silicon melt outside the partition of the crucible. And, in the above-mentioned apparatus, there is provided a supplying device for granular silicon raw material, which is provided with a falling speed reducing section for the granular silicon raw material in the middle of the guide tube.
[作 用]
案内管の先端部に遮蔽部を設けたことにより、投入され
た粒状シリコン原料がシリコン融液に当ってはね返って
も遮蔽部に当って再び仕切りの外側に落下し、仕切りの
内側に侵入することはない。[Function] By providing a shielding part at the tip of the guide tube, even if the introduced granular silicon raw material hits the silicon melt and rebounds, it will hit the shielding part and fall again to the outside of the partition, and it will fall inside the partition. will not invade.
また、案内管の途中に落下速度減速部を設けることによ
り、粒状シリコン原料の落下速度を減速し、シリコン融
液の液面に当ったときのはね返りを少なくする。Further, by providing a falling speed reducing part in the middle of the guide tube, the falling speed of the granular silicon raw material is reduced, and the rebound when it hits the surface of the silicon melt is reduced.
[発明の実施例]
第1図は本発明に係る粒状シリコンの供給装置を備えた
シリコン単結晶製造装置の一例の断面図である。図にお
いて、1は石英製のるつぼで、支持軸3に回転かつ上下
動可能に支持された黒鉛るつぼ2内にセットされている
。4はるつぼ1内に設けられた石英製の仕切りリングで
、下部にはシリコン融液5の流通孔4aが設けられてお
り、上部はシリコン融液5の液面から僅かに露出してい
る。[Embodiments of the Invention] FIG. 1 is a cross-sectional view of an example of a silicon single crystal production apparatus equipped with a granular silicon supply apparatus according to the present invention. In the figure, reference numeral 1 denotes a crucible made of quartz, which is set in a graphite crucible 2 supported by a support shaft 3 so as to be rotatable and movable up and down. Reference numeral 4 denotes a partition ring made of quartz provided in the crucible 1. A flow hole 4a for the silicon melt 5 is provided in the lower part of the partition ring 4, and the upper part is slightly exposed from the surface of the silicon melt 5.
るつぼ1はこの仕切りリング4により内側の単結晶育成
部Aと、外側の原料供給部Bとに分けられている。6は
シリコン融液5から引上げられた柱状シリコン単結晶で
ある。7は黒鉛るつぼ2の外周に配置され、シリコン融
液を加熱するヒータ、8はヒータ7の外側に設けられた
断熱材、9は加熱炉のハウジングである。The crucible 1 is divided by this partition ring 4 into an inner single crystal growth section A and an outer raw material supply section B. 6 is a columnar silicon single crystal pulled from the silicon melt 5. Reference numeral 7 denotes a heater arranged around the outer periphery of the graphite crucible 2 to heat the silicon melt, 8 a heat insulating material provided outside the heater 7, and 9 a housing of the heating furnace.
10はハウジング9の内外に設けられた粒状シリコン原
料の供給装置で、11はホッパー 12は一端がホッパ
ー11に連結された案内管である。案内管12は第2図
に示すように、先端部に案内管12の下部の径より大き
い円板状の遮蔽部13が設けられている。この遮蔽部1
3は、その下面をシリコン融液5の液面に可能な限り接
近して配置する事が望ましく、実施例では、遮蔽部13
の下面とシリコン融液5の液面との距離は5龍であった
。Reference numeral 10 represents a supply device for supplying granular silicon raw material provided inside and outside the housing 9, reference numeral 11 represents a hopper, and reference numeral 12 represents a guide tube connected to the hopper 11 at one end. As shown in FIG. 2, the guide tube 12 is provided with a disc-shaped shielding portion 13 at its tip end, the diameter of which is larger than the diameter of the lower portion of the guide tube 12. As shown in FIG. This shielding part 1
3 is desirably arranged with its lower surface as close as possible to the liquid surface of the silicon melt 5, and in the embodiment, the shielding part 13
The distance between the lower surface of the silicon melt 5 and the liquid level of the silicon melt 5 was 5 long.
次に、上記のように構成したシリコン単結晶製造装置の
作用を説明する。先ず、るつぼ1内に塊状のシリコン多
結晶を装入し、ヒータ7によりるつぼ1を加熱して溶解
する。ついで、種結晶を下降させて単結晶育成部Aのシ
リコン融液5の液面に接触させ、回転しながら徐々に引
上げると、柱状のシリコン単結晶6が育成される。一方
、原料の供給装置IOから案内管12を介して、シリコ
ン単結晶6の引上げ量に見合った量の粒状シリコン原料
を原料供給部Bに投入する。投入された粒状シリコン原
料は直ちに溶解し、シリコン単結晶6の引上げ量に見合
ったシリコン融液5が流通孔4aから単結晶育成部Aに
移動し、単結晶育成部Aと単結晶供給部Bのシリコン融
液5の液面を常に一定に保持する。Next, the operation of the silicon single crystal manufacturing apparatus configured as described above will be explained. First, a lump of silicon polycrystal is charged into the crucible 1, and the crucible 1 is heated by the heater 7 to melt it. Next, the seed crystal is lowered and brought into contact with the surface of the silicon melt 5 in the single crystal growth section A, and is gradually pulled up while rotating, thereby growing a columnar silicon single crystal 6. On the other hand, a granular silicon raw material in an amount commensurate with the amount of silicon single crystal 6 pulled is introduced into the raw material supply section B from the raw material supply device IO through the guide pipe 12. The input granular silicon raw material is immediately melted, and the silicon melt 5 corresponding to the amount of silicon single crystal 6 pulled moves from the flow hole 4a to the single crystal growth section A, and is then transferred to the single crystal growth section A and the single crystal supply section B. The liquid level of the silicon melt 5 is always kept constant.
ところで、本発明においては原料供給装置の案内管12
を前記のように構成したので、粒状シリコン原料がシリ
コン融液5の液面に落下してはね返っても遮蔽部13に
当り、再び原料供給部B内に落下して溶解するので、単
結晶育成部Aに侵入するおそれは全くない。By the way, in the present invention, the guide pipe 12 of the raw material supply device
is configured as described above, even if the granular silicon raw material falls onto the surface of the silicon melt 5 and bounces off, it will hit the shielding part 13 and fall into the raw material supply part B again and be melted, thereby preventing single crystal growth. There is no risk of it entering Part A.
なお、本実施例において、遮蔽部18のるつぼ1の半径
方向と直交する側、したがってるつぼ1の回転方向の両
側を第2図(b)に1点鎖線で示すように切除して小判
状に形成してもよい。In this embodiment, the side of the shielding part 18 perpendicular to the radial direction of the crucible 1, that is, both sides of the crucible 1 in the rotational direction, are cut off as shown by the dashed line in FIG. 2(b) to form an oval shape. may be formed.
第3図は本発明に係る遮蔽部13の別の実施例を示すも
ので、案内管12の下部に外管14を設け、その下端部
を案内管12の下端部より下方に位置させたものである
。FIG. 3 shows another embodiment of the shielding part 13 according to the present invention, in which an outer tube 14 is provided at the lower part of the guide tube 12, and its lower end is located below the lower end of the guide tube 12. It is.
また、第4図は本発明に係る遮蔽部13のさらに別の実
施例を示したものである。15は外壁がかまぼこ状に形
成され、るつぼ1の回転方向の両側に開口部16が設け
られた遮蔽部13を、その下端部が案内管12の下端部
より下方に位置するように案内管12に取付けたもので
、粒状シリコン原料を大量に投入する場合に実施して特
に有効である。Further, FIG. 4 shows still another embodiment of the shielding part 13 according to the present invention. 15 is a shielding part 13 whose outer wall is formed in a semicylindrical shape and has openings 16 on both sides in the rotational direction of the crucible 1, and which is connected to the guide tube 12 so that its lower end is located below the lower end of the guide tube 12. This is especially effective when a large amount of granular silicon raw material is introduced.
なお、第4図の実施例においては、遮蔽部13を原料供
給部Bのシリコン融液5内に浸漬した状態で、粒状シリ
コン原料を供給してもよい。In the embodiment shown in FIG. 4, the granular silicon raw material may be supplied while the shielding part 13 is immersed in the silicon melt 5 of the raw material supply part B.
次に、第1図で説明した本発明に係る原料供給装置と、
第6図に示す従来の原料供給装置(実開昭59−141
578号公報に開示された考案に相当するもの)とをそ
れぞれ使用して実験した結果を説明する。Next, the raw material supply device according to the present invention explained in FIG.
Conventional raw material supply device shown in Fig. 6
The results of experiments using the devices (corresponding to the device disclosed in Japanese Patent No. 578) will be explained.
先ず、第6図に示すように先端部を長さ方向と直角に切
断したまNの案内管12を有する原料供給装置lOによ
り、粒状シリコン原料を原料供給Bに連続的に投入した
ところ、多量の粒状シリコン原料が飛散して単結晶育成
部Aにはいり込み、成長中の単結晶6は直ちに多結晶化
してしまった。なお、この場合、案内管12の先端部と
、シリコン融液5の液面間との距離は30 m+*であ
った。First, as shown in FIG. 6, when a granular silicon raw material was continuously introduced into the raw material supply B using the raw material supply device 10 having the N guide tube 12 with its tip cut at right angles to the length direction, a large amount The granular silicon raw material was scattered and entered the single crystal growth section A, and the growing single crystal 6 immediately became polycrystalline. In this case, the distance between the tip of the guide tube 12 and the surface of the silicon melt 5 was 30 m+*.
次に第7図に示すように案内管12の先端部を斜めに切
除してその傾斜面をるつぼ1の内壁に対向させ、かつ先
端部をシリコン融液5の液面に可及的に近接(実験例で
は両者間の距離は5mm)させて配置し、粒状シリコン
原料を原料供給装置に連続的に投入した。その結果、大
部分の粒状シリコン原料は原料供給部Bに落下したが、
やはりその一部はシリコン融液5の液面ではねて単結晶
育成部Aにはいり込んだ。本例においては、シリコン単
結晶6は粒状シリコン原料を投入しはじめてから、暫く
終ったのち多結晶化した。Next, as shown in FIG. 7, the tip of the guide tube 12 is cut obliquely so that the inclined surface faces the inner wall of the crucible 1, and the tip is brought as close as possible to the surface of the silicon melt 5. (In the experimental example, the distance between the two was 5 mm), and the granular silicon raw material was continuously introduced into the raw material supply device. As a result, most of the granular silicon raw material fell into raw material supply section B, but
As expected, some of it splashed on the surface of the silicon melt 5 and entered the single crystal growth section A. In this example, the silicon single crystal 6 became polycrystalline some time after the introduction of the granular silicon raw material.
本発明に係る原料供給装置による実験結果は前述の通り
で、粒状シリコン原料の単結晶育成部Aへのはいり込み
は皆無であり、したがって長時間操業を続けてもシリコ
ン単結晶6が多結晶に転化することはなかった。The experimental results using the raw material supply device according to the present invention are as described above, and there is no intrusion of granular silicon raw material into the single crystal growth section A, so even if the operation continues for a long time, the silicon single crystal 6 becomes polycrystalline. There was no conversion.
第5図は本発明の別の実施例の断面図である。FIG. 5 is a cross-sectional view of another embodiment of the invention.
30は案内管12aの大径部内に設けられた粒状シリコ
ン原料の落下速度減速部で、漏斗状のシュート31と、
このシュート31に複数本の支持枠32で支持された、
案内管12aの大径部の内径より若干小径、上面半球状
で逆皿状の分配板33とから構成されている。30 is a falling speed reducing part of the granular silicon raw material provided in the large diameter part of the guide tube 12a, which includes a funnel-shaped chute 31;
This chute 31 is supported by a plurality of support frames 32,
It is composed of a distribution plate 33 having a slightly smaller diameter than the inner diameter of the large diameter portion of the guide tube 12a, and a hemispherical upper surface and an inverted dish shape.
このように構成した落下速度減速部30を備えた案内管
12aにおいては、原料供給装置lOから投入された粒
状シリコン原料は、シュート31によって整流されて分
配板33上に落下する。これにより落下のエネルギが減
衰した粒状シリコン原料は、分配板33の上面を転がり
ながら下降し、案内管12aの内壁と分配板33の外周
とで形成するすき間を通って原料0(給部Bの溶畿液面
上に落下する。このようにして、原料供給装置10から
落下した粒状シリコン原料の落下速度は落下速度減速部
30で零付近まで減速され、再び落下するのでシリコン
融液5の液面に落下したときの落下速度は大幅に減速さ
れ、したがって飛散を防止することができる。In the guide tube 12a equipped with the falling speed reducing section 30 configured in this way, the granular silicon raw material introduced from the raw material supply device IO is rectified by the chute 31 and falls onto the distribution plate 33. As a result, the granular silicon raw material whose falling energy has been attenuated descends while rolling on the upper surface of the distribution plate 33, passes through the gap formed between the inner wall of the guide tube 12a and the outer periphery of the distribution plate 33, and passes through the raw material 0 (supply section B). In this way, the falling speed of the granular silicon raw material that has fallen from the raw material supply device 10 is reduced to near zero by the falling speed reduction section 30, and the silicon melt 5 falls again. The falling speed when falling onto a surface is significantly reduced, thus preventing scattering.
上記の実施例では、第1図に示したシリコン単結晶の製
造装置に本発明を実施した場合を示したが、シリコン単
結晶を引上げながら粒状シリコン原料を投入する方式の
装置であれば、他の構成のものにも本発明を実施するこ
とができる。また、遮蔽部は落下速度減速部を備えた案
内管に設けてもよく、あるいは落下速度減速部のない案
内管に設けてもよい。さらに遮蔽部の構造は前記実施例
に限定するものではなく、落下した粒状シリコン原料が
シリコン融液の液面に当ってはね返り、単結晶育成部に
侵入するものを防止できるものであれば、他の構造のも
のでもよい。In the above embodiment, the present invention was applied to the silicon single crystal manufacturing apparatus shown in FIG. The present invention can also be implemented in the configuration of. Further, the shielding portion may be provided on a guide tube provided with a falling speed reducing portion, or may be provided on a guide tube without a falling speed reducing portion. Furthermore, the structure of the shielding part is not limited to the above-mentioned embodiment, and any structure can be used as long as it can prevent the fallen granular silicon raw material from hitting the liquid surface of the silicon melt and rebounding and entering the single crystal growth part. It may have the structure of
[発明の効果]
以上の説明から明らかなように、本発明は原料供給部に
粒状シリコン原料を供給する案内管の先端部に遮蔽部を
設けて、投入された粒状シリコン原料が単結晶育成部に
侵入するのを防止するようにしたので、育成されるシリ
コン単結晶が有転位化することを防止できる。このため
頭部から足部にかけてドープ剤濃度の均一な高品質のシ
リコン単結晶を得ることができる。[Effects of the Invention] As is clear from the above description, the present invention provides a shielding portion at the tip of the guide tube that supplies the granular silicon raw material to the raw material supply section, so that the granular silicon raw material fed into the single crystal growth section Since it is possible to prevent the silicon single crystal being grown from becoming dislocated. Therefore, a high quality silicon single crystal with a uniform dopant concentration from the head to the foot can be obtained.
また、上記の案内管の途中に、粒状シリコン原料の落下
速度減速部を設けることにより、投入される粒状シリコ
ン原料の落下速度を低減し、シリコン融液の液面に当っ
たときのはね返りを小さくし、単結晶育成部への侵入防
止をさらに確実にする。In addition, by providing a part that reduces the falling speed of the granular silicon raw material in the middle of the guide tube, the falling speed of the granular silicon raw material being introduced is reduced, and the rebound when it hits the surface of the silicon melt is reduced. This further ensures prevention of intrusion into the single crystal growth section.
第1図は本発明に係る原料供給装置を備えたシリコン単
結晶製造装置の一例の模式図、第2図及び第3図は本発
明要部の実施例を示すもので、それぞれ(a)は一部を
断面で示した正面図、(b)は底面図、第4図は本発明
要部の他の実施例を示すもので、(a)は斜視図、(b
)は底面図、第5図は本発明の別の実施例を示す断面図
、第6図は従来のシリコン単結晶の製造装置の一例を示
す模式図、第7図はさらに他の例の要部を示す模式図で
ある。
1:るつぼ、4:仕切りリング、5:シリコン融液、6
:シリコン単結晶、7:ヒータ、10:原料供給装置、
12.12a:案内管、13:遮蔽部、30:落下速度
減速部、A:単結晶育成部、B:原料供給部。
代理人 弁理士 佐々木 宗 治
慨
図
第5図FIG. 1 is a schematic diagram of an example of a silicon single crystal manufacturing apparatus equipped with a raw material supply device according to the present invention, and FIGS. 2 and 3 show an embodiment of the main part of the present invention. (b) is a bottom view, FIG. 4 shows another embodiment of the main part of the present invention, (a) is a perspective view, (b)
) is a bottom view, FIG. 5 is a sectional view showing another embodiment of the present invention, FIG. 6 is a schematic diagram showing an example of a conventional silicon single crystal manufacturing apparatus, and FIG. 7 is a schematic diagram of another example. FIG. 1: Crucible, 4: Partition ring, 5: Silicon melt, 6
: Silicon single crystal, 7: Heater, 10: Raw material supply device,
12.12a: Guide tube, 13: Shielding section, 30: Falling speed reduction section, A: Single crystal growth section, B: Raw material supply section. Agent Patent Attorney So Sasaki Chart Diagram 5
Claims (2)
切りの内側からシリコン単結晶を引上げると共に、前記
仕切りの外側に案内管により粒状シリコン原料を連続的
に供給してシリコン単結晶を製造する装置において、 前記案内管の先端部に該案内管の外径より大きい遮蔽部
を設け、該遮蔽部を前記るつぼの仕切りの外側のシリコ
ン融液の液面に近接し又はその一部を浸漬して配置した
ことを特徴とする粒状シリコン原料の供給装置。(1) A crucible having a ring-shaped partition is provided, and a silicon single crystal is pulled up from inside the partition, and a granular silicon raw material is continuously supplied to the outside of the partition through a guide tube to produce a silicon single crystal. In the apparatus, a shielding portion larger than the outer diameter of the guide tube is provided at the tip of the guide tube, and the shielding portion is placed close to the liquid surface of the silicon melt outside the partition of the crucible or a part thereof is immersed. A supply device for a granular silicon raw material, characterized in that the device is arranged at
下速度減速部を設けたことを特徴とする請求項(1)記
載の粒状シリコン原料の供給装置。(2) The apparatus for supplying granular silicon raw material according to claim 1, characterized in that a part for reducing the falling speed of the granular silicon raw material is provided in the middle of the guide tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16508488A JPH0218376A (en) | 1988-07-04 | 1988-07-04 | Granular silicon raw material supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16508488A JPH0218376A (en) | 1988-07-04 | 1988-07-04 | Granular silicon raw material supply device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0218376A true JPH0218376A (en) | 1990-01-22 |
Family
ID=15805573
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16508488A Pending JPH0218376A (en) | 1988-07-04 | 1988-07-04 | Granular silicon raw material supply device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0218376A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0597570A (en) * | 1991-10-11 | 1993-04-20 | Nkk Corp | Silicon single crystal manufacturing apparatus and manufacturing method |
| JPH0612477U (en) * | 1992-07-24 | 1994-02-18 | 三菱マテリアル株式会社 | Lifting device |
-
1988
- 1988-07-04 JP JP16508488A patent/JPH0218376A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0597570A (en) * | 1991-10-11 | 1993-04-20 | Nkk Corp | Silicon single crystal manufacturing apparatus and manufacturing method |
| JPH0612477U (en) * | 1992-07-24 | 1994-02-18 | 三菱マテリアル株式会社 | Lifting device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5087321A (en) | Manufacturing method and equipment of single silicon crystal | |
| JP4225688B2 (en) | Method for producing a silicon melt from a polysilicon charge | |
| CA1261715A (en) | Apparatus and process for growing monocrystals of semiconductor materials from shallow crucibles by czochralski technique | |
| US5087429A (en) | Method and apparatus for manufacturing silicon single crystals | |
| JPH0676274B2 (en) | Silicon single crystal manufacturing equipment | |
| KR100800212B1 (en) | Apparatus and method for supplying a solid raw material to a single crystal growth apparatus | |
| US5367981A (en) | Apparatus for manufacturing crystals through floating zone method | |
| KR20050044493A (en) | Intermittent feeding technique for increasing the melting rate of polycrystalline silicon | |
| JP2688137B2 (en) | Method of pulling silicon single crystal | |
| JPH0218376A (en) | Granular silicon raw material supply device | |
| JP7052912B1 (en) | Single crystal pulling device | |
| JPH0764672B2 (en) | Crystal growth equipment | |
| JP2681115B2 (en) | Single crystal manufacturing method | |
| JP3085565B2 (en) | Recharge method in semiconductor single crystal pulling | |
| JPH01317189A (en) | Production of single crystal of silicon and device therefor | |
| JP2024520171A (en) | Use of quartz plates during the growth of monocrystalline silicon ingots | |
| JP4075136B2 (en) | Single crystal growth equipment | |
| JPH07110798B2 (en) | Single crystal manufacturing equipment | |
| JPH0723277B2 (en) | Crystal growth equipment | |
| CN218666397U (en) | Wear monitoring system, lifting mechanism and crystal pulling furnace | |
| JPS63319288A (en) | Flanged quartz crucible | |
| JPH0316989A (en) | Silicon single crystal production equipment | |
| JPH0733583A (en) | Apparatus for growing semiconductor single crystal | |
| JPH0280392A (en) | Single crystal production device | |
| JP2732750B2 (en) | Doping device for CZ single crystal |