JP5941384B2 - Method for producing silica glass crucible for pulling silicon single crystal - Google Patents
Method for producing silica glass crucible for pulling silicon single crystal Download PDFInfo
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- JP5941384B2 JP5941384B2 JP2012210534A JP2012210534A JP5941384B2 JP 5941384 B2 JP5941384 B2 JP 5941384B2 JP 2012210534 A JP2012210534 A JP 2012210534A JP 2012210534 A JP2012210534 A JP 2012210534A JP 5941384 B2 JP5941384 B2 JP 5941384B2
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Description
本発明は、チョクラルスキー法(以下、CZ法という)によりシリコン単結晶を引上げる際に用いられる、原料シリコン融液を収容するためのシリカガラスルツボの製造方法に関する。より詳しくは、シリコン単結晶を引上げる際に発生するルツボ内層の気泡発生および膨張を抑制することによって、歩留まり良くシリコン単結晶を引上げることができるシリカガラスルツボの製造方法に関するものである。 The present invention relates to a method for producing a silica glass crucible for containing a raw material silicon melt used when pulling up a silicon single crystal by the Czochralski method (hereinafter referred to as CZ method). More specifically, the present invention relates to a method for producing a silica glass crucible that can pull up a silicon single crystal with a high yield by suppressing bubble generation and expansion in the inner layer of the crucible that is generated when pulling up the silicon single crystal.
シリコン単結晶の製造においては、チョクラルスキー法(CZ法)が広く用いられている。この方法は、ルツボ内に収容された原料シリコン融液の表面に種結晶を接触させ、ルツボを回転させるとともに、前記種結晶を反対方向に回転させながら上方へ引上げることにより、種結晶の下端に単結晶インゴットを育成していくものである。 The Czochralski method (CZ method) is widely used in the production of silicon single crystals. In this method, the seed crystal is brought into contact with the surface of the raw material silicon melt contained in the crucible, the crucible is rotated, and the seed crystal is pulled upward while rotating the seed crystal in the opposite direction. Single crystal ingots are nurtured.
上記方法において、原料シリコン融液を収容するためのルツボには、シリカガラスルツボが用いられる。このシリカガラスルツボは、一般に、特許文献1に開示されているような2層構造であり、外層が不透明層、内層が透明層である。
前記外層の不透明層は、合成シリカガラスに比べて、純度は低いものの、耐熱性に優れた天然シリカ原料により形成され、多数の気泡を含有している。一方、前記内層の透明層は、引上げられるシリコン単結晶インゴットに対する不純物汚染の抑制のため、高純度の合成シリカ原料により形成され、また、前記単結晶インゴットの結晶化率の向上等の観点から、ルツボ内表面は平滑に形成される。
このようなシリカガラスルツボの前記内層はシリコン単結晶引上げ開始前において実質的に無気泡の透明層であるが、シリコン単結晶引上げのために減圧、高温に曝されると気泡が生じ、その気泡が膨張することによりルツボ内表面が剥離する、もしくは気泡内部のガスがガス泡となって原料シリコン融液内に放出されることがある。この剥離片やガス泡が原料シリコン融液の対流によりシリコン単結晶の成長界面に到達し、取り込まれるとシリコン単結晶の品質を低下させるという問題があった。
In the above method, a silica glass crucible is used as a crucible for containing the raw material silicon melt. This silica glass crucible generally has a two-layer structure as disclosed in Patent Document 1, with the outer layer being an opaque layer and the inner layer being a transparent layer.
The outer opaque layer has a lower purity than synthetic silica glass, but is formed of a natural silica material excellent in heat resistance and contains a large number of bubbles. On the other hand, the transparent layer of the inner layer is formed of a high-purity synthetic silica raw material in order to suppress impurity contamination on the pulled silicon single crystal ingot, and from the viewpoint of improving the crystallization rate of the single crystal ingot, etc. The inner surface of the crucible is formed smoothly.
The inner layer of such a silica glass crucible is a substantially bubble-free transparent layer before starting the pulling of the silicon single crystal, but bubbles are generated when exposed to reduced pressure and high temperature for pulling the silicon single crystal. In some cases, the inner surface of the crucible peels due to expansion of the gas, or the gas inside the bubbles becomes gas bubbles and is released into the raw silicon melt. There has been a problem that the quality of the silicon single crystal is lowered when the peeled pieces and gas bubbles reach the growth interface of the silicon single crystal by convection of the raw material silicon melt and are taken in.
上記問題を解決するため、加熱溶融して半透明石英ガラスルツボ基体の内面側に、水素ドープシリカ粉および水素未ドープ石英粉により透明石英ガラス層を形成する、例えば、特許文献2に記載されているような石英ガラスルツボの製造方法が提案されている。また、特許文献3には、引上げ相当温度下において、内表面透明層に含まれる気泡の膨張率を制御した石英ガラスルツボが開示されている。 In order to solve the above-mentioned problem, a transparent quartz glass layer is formed by heating and melting the hydrogen-doped silica powder and the hydrogen-undoped quartz powder on the inner surface side of the translucent quartz glass crucible base. A method for producing such a quartz glass crucible has been proposed. Patent Document 3 discloses a quartz glass crucible in which the expansion rate of bubbles contained in the inner surface transparent layer is controlled at a pulling equivalent temperature.
しかしながら、上記のような石英ガラスルツボを用いた場合であっても、CZ法によるシリコン単結晶引上げの際、原料シリコンを溶融、保持している状態で透明層内に気泡が生じ、膨張することがあった。膨張した気泡が原料シリコン融液と接するルツボ内表面に開放した場合、ガス泡やシリカガラス小片が原料シリコン融液に混入し、原料シリコン融液の対流によってシリコン単結晶の引上げ界面に到達してシリコン単結晶内に取り込まれてしまうことがある。ガス泡が取り込まれた場合、引上げたシリコン単結晶の外観からは不具合を確認することはできず、シリコン単結晶をスライス、研磨してシリコンウェーハとした後にピンホール、異物欠陥などとして見つかる。シリカガラス小片が取り込まれた場合、引上げたシリコン単結晶に転位が起こりシリコン単結晶の品質が低下する。 However, even when the quartz glass crucible as described above is used, when the silicon single crystal is pulled by the CZ method, bubbles are generated in the transparent layer in a state where the raw material silicon is melted and held and expands. was there. When the expanded bubbles open to the inner surface of the crucible in contact with the raw material silicon melt, gas bubbles and silica glass fragments enter the raw material silicon melt and reach the pulling interface of the silicon single crystal by the convection of the raw material silicon melt. In some cases, it is taken into the silicon single crystal. When the gas bubbles are taken in, the defect cannot be confirmed from the appearance of the pulled silicon single crystal, and it is found as a pinhole, foreign object defect, etc. after slicing and polishing the silicon single crystal to form a silicon wafer. When the silica glass piece is taken in, dislocation occurs in the pulled silicon single crystal and the quality of the silicon single crystal is deteriorated.
使用前の実質的に無気泡の透明層においては、どこに気泡が生じるか、どの程度膨張するかを確認することはできず、使用中の気泡発生、膨張を制御できないという課題が生じていた。 In the substantially bubble-free transparent layer before use, it is impossible to confirm where the bubbles are generated and how much the bubbles are expanded, and there is a problem that the generation and expansion of bubbles during use cannot be controlled.
こうした現状を鑑み、本発明者は、鋭意研究を重ねた結果、透明層内での気泡発生、膨張は透明層のシリカガラス中の酸素過剰欠陥に起因し、酸素過剰欠陥はアーク放電による加熱溶融の際にシリカガラス構造内に取り込まれた酸素によって増加していることを見出した。
アーク放電による加熱溶融の際、カーボン電極から生じるカーボン粒子がルツボ内表面に付着することを防止するため、加熱溶融中の酸素供給をなくすることはできないが、ルツボ内表面に沿って水素を供給することにより酸素過剰欠陥を抑制することができることを見出して、本発明を完成したものである。
In view of the current situation, the present inventor has conducted extensive research, and as a result, bubble generation and expansion in the transparent layer are caused by oxygen excess defects in the silica glass of the transparent layer, and oxygen excess defects are heated and melted by arc discharge. It was found that the oxygen was increased by oxygen incorporated into the silica glass structure.
In order to prevent carbon particles generated from the carbon electrode from adhering to the inner surface of the crucible during heating and melting by arc discharge, oxygen supply during heating and melting cannot be eliminated, but hydrogen is supplied along the inner surface of the crucible. Thus, the present invention has been completed by finding that oxygen excess defects can be suppressed.
すなわち、本発明は、内層である透明層において、使用中すなわちルツボ内部に収容した多結晶シリコンを溶融するために加熱を開始してからシリコン単結晶の引上げ終了までの間、気泡の発生および膨張を抑制することのできる、シリコン単結晶引上げ用シリカガラスルツボを提供することを目的とするものである。 That is, according to the present invention, in the transparent layer which is the inner layer, bubbles are generated and expanded during use, that is, from the start of heating to melt the polycrystalline silicon contained in the crucible until the end of pulling of the silicon single crystal. An object of the present invention is to provide a silica glass crucible for pulling up a silicon single crystal capable of suppressing the above.
本発明に係るシリコン単結晶引上げ用シリカガラスルツボの製造方法は、石英原料粉末を成形型内に供給して直胴部、コーナー部および底部を有するシリカ粉成形体を形成し、このシリカ粉成形体をアーク放電により加熱溶融してシリカガラスルツボを得る製造方法であって、酸素雰囲気中でのアーク放電による加熱溶融の際に、シリカ粉成形体の直胴部内表面に沿って水素ガスを供給することを特徴とする。
このような製造方法によれば、加熱溶融中において透明層のシリカガラス構造内に酸素を取り込むことを抑制し、透明層内の酸素過剰欠陥を少なくすることができる。
The method for producing a silica glass crucible for pulling up a silicon single crystal according to the present invention supplies a quartz raw material powder into a molding die to form a silica powder molded body having a straight body portion, a corner portion and a bottom portion, and this silica powder molding This is a manufacturing method for obtaining a silica glass crucible by heating and melting the body by arc discharge, and supplying hydrogen gas along the inner surface of the straight body of the silica powder molded body during heating and melting by arc discharge in an oxygen atmosphere It is characterized by doing.
According to such a manufacturing method, it is possible to suppress oxygen from being taken into the silica glass structure of the transparent layer during heating and melting, and to reduce oxygen excess defects in the transparent layer.
前記シリコン単結晶引上げ用シリカガラスルツボの製造方法においては、水素ガスの供給量を40リットル/min以上60リットル/min以下とすることが好ましい。
水素流量をこのような範囲とすることにより、シリカガラス中のOH濃度が増加して透明層の高温強度が低下することなく、加熱溶融中において透明層のシリカガラス構造内に酸素を取り込むことを抑制し、透明層内の酸素過剰欠陥を少なくすることができる。
In the method for producing a silica glass crucible for pulling a silicon single crystal, the supply amount of hydrogen gas is preferably 40 liter / min or more and 60 liter / min or less.
By setting the hydrogen flow rate in such a range, the OH concentration in the silica glass is increased and the high-temperature strength of the transparent layer is not lowered, and oxygen is taken into the silica glass structure of the transparent layer during heating and melting. It is possible to suppress and reduce oxygen excess defects in the transparent layer.
本発明に係るシリコン単結晶引上げ用シリカガラスルツボの製造方法によれば、加熱溶融中において実質的に無気泡の透明層のシリカガラス構造内に酸素を取り込むことを抑制し、透明層内の酸素過剰欠陥を少なくすることにより、シリコン単結晶引上げ中における気泡膨張を抑制することができる。 According to the method for producing a silica glass crucible for pulling up a silicon single crystal according to the present invention, it is possible to suppress oxygen from being taken into the silica glass structure of a substantially bubble-free transparent layer during heating and melting, and oxygen in the transparent layer. By reducing excessive defects, bubble expansion during pulling of the silicon single crystal can be suppressed.
本発明にかかる製造方法により得られるシリコン単結晶引上げ用シリカガラスルツボ1は、図1に示すように、底部と円筒状の側壁部との間にアール状のコーナー部を有する断面がU字状の形状からなる。そして、外層3が不透明層、内層2が透明層からなる。
ここで、不透明層とは、シリカガラス中に多数の気泡(好ましくは、20個/mm3以上)を含み、見かけ上、白濁した状態のシリカガラス層であり、透明層とは、シリカガラス中に気泡をほとんど含まず(好ましくは、2個/mm3以下)、実質的に透明であるシリカガラス層を意味する。
As shown in FIG. 1, a silica glass crucible 1 for pulling a silicon single crystal obtained by the manufacturing method according to the present invention has a U-shaped cross section having a rounded corner portion between a bottom portion and a cylindrical side wall portion. It consists of the shape. The outer layer 3 is an opaque layer and the inner layer 2 is a transparent layer.
Here, the opaque layer is a silica glass layer that contains many bubbles (preferably 20 / mm 3 or more) in the silica glass and is apparently clouded, and the transparent layer is in the silica glass. Means a silica glass layer substantially free of bubbles (preferably 2 / mm 3 or less) and substantially transparent.
本発明にかかるシリコン単結晶引上げ用シリカガラスルツボの製造方法は、酸素雰囲気中でのアーク放電による加熱溶融の際に、シリカ粉成形体の直胴部内表面に沿うように水素ガスを供給する点に特徴があり、シリカガラスルツボの製造方法は従来の一般的な方法が用いられる。
なお、一般に、不透明層は、純度は低いものの、耐熱性に優れた、水晶等の天然シリカ原料により形成し、透明層は、シリコンアルコキシドの加水分解等により得られる高純度の合成シリカ原料により形成する。
The method for producing a silica glass crucible for pulling up a silicon single crystal according to the present invention is characterized in that hydrogen gas is supplied along the inner surface of a straight body portion of a silica powder molded body during heating and melting by arc discharge in an oxygen atmosphere. The conventional general method is used as the method for producing the silica glass crucible.
In general, the opaque layer is formed of a natural silica material such as quartz, which is low in purity but excellent in heat resistance, and the transparent layer is formed of a high-purity synthetic silica material obtained by hydrolysis of silicon alkoxide. To do.
図2に示すようなシリカガラスルツボ製造装置を用いて、図示しない回転駆動源を稼働して回転軸15を矢印の方向に、ルツボ成形用型11を高速で回転させつつ、ルツボ成形用型11内の上部から、初めに天然シリカ原料粉末を装填し、さらにその内表面に合成シリカ原料粉末を装填する。 Using a silica glass crucible manufacturing apparatus as shown in FIG. 2, a crucible molding die 11 is operated while operating a rotational drive source (not shown) and rotating the crucible molding die 11 at a high speed in the direction of the arrow. First, natural silica raw material powder is charged from the upper part inside, and further, synthetic silica raw material powder is charged on the inner surface thereof.
初めに供給された天然シリカ原料粉末は、遠心力によってルツボ成形用型11の内側部材12に押圧され、一つの天然シリカ原料粉末層20bが形成される。
そして、この天然シリカ原料粉末に続いて合成シリカ原料粉末がルツボ成形用型11内に供給され、合成シリカ原料粉末は、遠心力によって天然シリカ原料粉末の層に押圧され一つの合成シリカ原料粉末層20aが形成され、全体としてルツボ形状の2層のシリカ粉成形体20が形成される。
その後、大気雰囲気において減圧機構18の作動により減圧し、カーボン電極19に通電してシリカ粉成形体20の内側から加熱し、シリカ粉成形体20を内側から順次溶融する。カーボン電極19の通電開始後、シリカ粉成形体20の開口部から直胴部内表面に沿って水素ガスの供給を開始し、カーボン電極19の通電終了後に水素ガスの供給を止める。
The initially supplied natural silica raw material powder is pressed against the inner member 12 of the crucible molding die 11 by centrifugal force to form one natural silica raw material powder layer 20b.
Then, following this natural silica raw material powder, a synthetic silica raw material powder is supplied into the crucible molding die 11, and the synthetic silica raw material powder is pressed against the natural silica raw material powder layer by centrifugal force to form one synthetic silica raw material powder layer. 20a is formed, and a two-layered silica powder molded body 20 having a crucible shape as a whole is formed.
Thereafter, the pressure is reduced by the operation of the pressure reducing mechanism 18 in the air atmosphere, the carbon electrode 19 is energized and heated from the inside of the silica powder molded body 20, and the silica powder molded body 20 is sequentially melted from the inside. After the energization of the carbon electrode 19 is started, the supply of hydrogen gas is started from the opening of the silica powder molded body 20 along the inner surface of the straight body portion, and the supply of the hydrogen gas is stopped after the energization of the carbon electrode 19 is completed.
その後、冷却することにより、内面側には実質的に無気泡化状態で酸素過剰欠陥が抑制された透明シリカガラス層2が形成され、外表側には多数の気泡が存在する不透明シリカガラス層3が形成された、2重層構造のシリカガラスルツボ1が製造される。 Thereafter, by cooling, a transparent silica glass layer 2 in which oxygen excess defects are suppressed in a substantially bubble-free state on the inner surface side, and an opaque silica glass layer 3 in which a large number of bubbles exist on the outer surface side is formed. A silica glass crucible 1 having a double layer structure is formed.
このように、水素ガスをシリカ粉成形体20の開口部から直胴部内表面に沿って供給することにより、酸素含有雰囲気中でのアーク放電による加熱溶融中において実質的に無気泡の透明層のシリカガラス構造内に酸素を取り込むことを抑制し、酸素過剰欠陥を少なくすることにより、シリコン単結晶引上げ中における気泡発生および発生した気泡の膨張を抑制することができる。 Thus, by supplying hydrogen gas from the opening of the silica powder molded body 20 along the inner surface of the straight body portion, a substantially bubble-free transparent layer is formed during heating and melting by arc discharge in an oxygen-containing atmosphere. By suppressing oxygen incorporation into the silica glass structure and reducing oxygen excess defects, it is possible to suppress bubble generation and expansion of the generated bubbles during pulling of the silicon single crystal.
水素ガスは、シリカ粉成形体20の開口部から直胴部内表面に沿って供給すること、できるだけカーボン電極19と接触しないように供給することが好ましい。供給した水素ガスがカーボン電極19と接触した場合、カーボン電極19から生じるカーボン粒子が雰囲気中の酸素と反応せずにルツボ内表面に付着してしまう。 It is preferable to supply the hydrogen gas from the opening of the silica powder molded body 20 along the inner surface of the straight body portion, and to supply the hydrogen gas so as not to contact the carbon electrode 19 as much as possible. When the supplied hydrogen gas comes into contact with the carbon electrode 19, carbon particles generated from the carbon electrode 19 do not react with oxygen in the atmosphere and adhere to the inner surface of the crucible.
また、水素ガスはできるだけシリカ粉成形体20に直接吹き付けないように供給することが好ましい。供給した水素ガスがシリカ粉成形体20に直接吹き付けられた場合、透明層となるシリカ粉成形体20の内表層に深く入り込んでしまい、透明層中のOH基濃度が高くなってしまう。 Further, it is preferable to supply the hydrogen gas so as not to be blown directly onto the silica powder molded body 20 as much as possible. When the supplied hydrogen gas is directly blown onto the silica powder molded body 20, it deeply penetrates into the inner surface layer of the silica powder molded body 20 to be a transparent layer, and the OH group concentration in the transparent layer becomes high.
供給する水素流量は40リットル/min以上60リットル/min以下とすることが好ましい。水素流量が40リットル/min未満である場合には、透明層の気泡発生および膨張を抑制する効果が小さくなり、引上げられたシリコン単結晶インゴットに転位やエアポケットなどの欠陥が生じる虞があるため好ましくない。一方、水素流量が60リットル/minを超えた場合には、透明層中のOH基濃度が高くなってしまい、透明層の高温強度が低下することにより変形し易くなるため好ましくない。 The supplied hydrogen flow rate is preferably 40 liters / min or more and 60 liters / min or less. When the hydrogen flow rate is less than 40 liters / min, the effect of suppressing the bubble generation and expansion of the transparent layer is reduced, and defects such as dislocations and air pockets may occur in the pulled silicon single crystal ingot. It is not preferable. On the other hand, when the hydrogen flow rate exceeds 60 liters / min, the OH group concentration in the transparent layer increases, and the high-temperature strength of the transparent layer is reduced, which is not preferable.
以下、本発明を実施例に基づいてさらに具体的に説明するが、本発明は下記実施例により制限されるものではない。
[実施例1]
上記の実施の形態において説明した方法と同様の製造方法により、外径約600mm、高さ約500mmのシリカ粉成形体を形成し、水素ガスを40リットル/minの流量で供給しながらアーク放電により加熱溶融してシリカガラスルツボを製造した。
このシリカガラスルツボを、カーボンルツボに嵌め込んでセットし、ルツボ外周からヒータ加熱して、ルツボ内で多結晶シリコン原料を溶融させ、CZ法により、直径8インチのシリコン単結晶引上げを行った。
EXAMPLES Hereinafter, although this invention is demonstrated further more concretely based on an Example, this invention is not restrict | limited by the following Example.
[Example 1]
By a manufacturing method similar to the method described in the above embodiment, a silica powder molded body having an outer diameter of about 600 mm and a height of about 500 mm is formed, and arc discharge while supplying hydrogen gas at a flow rate of 40 liters / min. A silica glass crucible was produced by heating and melting.
The silica glass crucible was fitted into a carbon crucible, set, heated with a heater from the outer periphery of the crucible, the polycrystalline silicon raw material was melted in the crucible, and a silicon single crystal having a diameter of 8 inches was pulled by the CZ method.
[実施例2]
上記実施例1において、水素ガスの流量を60リットル/minとした以外実施例1と同様にしてシリカガラスルツボを製造し、このルツボを用いて、実施例1と同様にして、シリコン単結晶引上げを行った。
[Example 2]
In Example 1 above, a silica glass crucible was produced in the same manner as in Example 1 except that the flow rate of hydrogen gas was changed to 60 liters / min. Using this crucible, in the same manner as in Example 1, the silicon single crystal was pulled up. Went.
[比較例1]
上記実施例1において、水素ガスを供給せずにシリカガラスルツボを製造し、このルツボを用いて、実施例1と同様にして、シリコン単結晶引上げを行った
[Comparative Example 1]
In Example 1 above, a silica glass crucible was produced without supplying hydrogen gas, and using this crucible, a silicon single crystal was pulled in the same manner as in Example 1.
[比較例2〜4]
水素ガスの流量を下記表1の比較例2〜4に示すように変化させ、それ以外は実施例1と同様にして、シリカガラスルツボを製造し、これらの各ルツボを用いて、実施例1と同様にして、シリコン単結晶引上げを行った。
[Comparative Examples 2 to 4]
A silica glass crucible was produced in the same manner as in Example 1 except that the flow rate of hydrogen gas was changed as shown in Comparative Examples 2 to 4 in Table 1 below. Example 1 was made using each of these crucibles. In the same manner, the silicon single crystal was pulled.
上記実施例及び比較例において製造したシリカガラスルツボについて、水素ガスを供給しなかった比較例1のシリカガラスルツボの透明層OH基含有量を基準としてOH基含有量の濃度増加量を評価した。また、シリコン単結晶引上げに使用した後の透明層気泡密度、引上げられたシリコン単結晶インゴットの結晶化率の評価を行った。
これらの評価結果をまとめて表1に示す。
About the silica glass crucible manufactured in the said Example and comparative example, the density | concentration increase amount of OH group content was evaluated on the basis of transparent layer OH group content of the silica glass crucible of the comparative example 1 which did not supply hydrogen gas. Further, the bubble density of the transparent layer after use for pulling the silicon single crystal and the crystallization rate of the pulled silicon single crystal ingot were evaluated.
These evaluation results are summarized in Table 1.
シリカガラスルツボ中のOH基濃度は赤外分光分析法により測定した。詳細には、まずシリカガラスルツボから透明層のみのシリカガラス片を切り出し、表面研磨して測定用サンプルとした。次に、赤外分光光度計(光透過率測定装置)を用いて、測定用サンプルの表面に赤外線を入射させ、測定用サンプルの裏面から出射した透過光を受光し、測定された赤外線の吸収スペクトルにおけるOH基に起因した赤外線吸収ピークを選択し、そのピークの波長における透過率と、赤外線吸収による影響を受けない波長における透過率とを比較することにより、透明層中のOH基濃度を算出した。 The OH group concentration in the silica glass crucible was measured by infrared spectroscopy. Specifically, first, a silica glass piece having only a transparent layer was cut out from a silica glass crucible, and the surface was polished to obtain a measurement sample. Next, using an infrared spectrophotometer (light transmittance measuring device), infrared light is incident on the surface of the measurement sample, the transmitted light emitted from the back surface of the measurement sample is received, and the measured infrared absorption Select the infrared absorption peak due to the OH group in the spectrum, and calculate the OH group concentration in the transparent layer by comparing the transmittance at the wavelength of the peak with the transmittance at a wavelength not affected by infrared absorption. did.
シリコン単結晶引上げ後のシリカガラスルツボに形成された気泡の密度の測定は、CCDカメラとハロゲンランプとを用い、ルツボ内表面からの画像を撮像し、得られた画像を二値化処理することにより行った。測定視野は、500μm2以上(好ましくは1.0mm×1.4mm)で、認識可能な最小気泡径は4.6μm以上とした。また、厚さ方向は、20μmピッチでCCDカメラを移動させることにより、表層から1.0mmの厚さまで測定した。
尚、この測定は、ルツボ周方向に略等間隔で4点(90°間隔)に対して行った。
The density of bubbles formed in the silica glass crucible after pulling the silicon single crystal is measured using a CCD camera and a halogen lamp to capture an image from the inner surface of the crucible and binarize the resulting image. It went by. The measurement field of view was 500 μm 2 or more (preferably 1.0 mm × 1.4 mm), and the recognizable minimum bubble diameter was 4.6 μm or more. The thickness direction was measured from the surface layer to a thickness of 1.0 mm by moving the CCD camera at a pitch of 20 μm.
This measurement was performed on four points (at intervals of 90 °) at substantially equal intervals in the circumferential direction of the crucible.
結晶化率は、用いた多結晶シリコン原料の量およびルツボ形状から算出し設定されたシリコン単結晶インゴットの長さ(直胴部、トップ部およびテール部を含む)に対する実際に引き上げられたシリコン単結晶インゴットの長さとして定義した。 The crystallization rate is calculated based on the amount of the polycrystalline silicon raw material used and the crucible shape, and the length of the silicon single crystal ingot (including the straight body portion, top portion, and tail portion) that is actually set is increased. It was defined as the length of the crystal ingot.
上記実施例及び比較例の結果から、酸素雰囲気中でのアーク放電による加熱溶融の際に、シリカ粉成形体の直胴部内表面に接するように水素ガスを40リットル/min以上60リットル/min以下の流量で供給することにより、透明層の気泡発生を抑制し、ルツボの変形は生じず、引上げられたシリコン単結晶インゴットの結晶化率も良好であった。 From the results of the above Examples and Comparative Examples, hydrogen gas was used in an amount of 40 liters / min or more and 60 liters / min or less so as to come into contact with the inner surface of the straight body portion of the silica powder molded body during heating and melting by arc discharge in an oxygen atmosphere. By supplying at a flow rate of, the generation of bubbles in the transparent layer was suppressed, the crucible was not deformed, and the crystallization rate of the pulled silicon single crystal ingot was good.
1 シリカガラスルツボ
2 透明シリカガラス層
3 不透明シリカガラス層
10 シリカガラスルツボ製造装置
11 ルツボ成形用型
12 内側部材
13 通気部
14 保持体
15 回転軸
16 開口部
17 排気口
18 減圧機構
19 カーボン電極
20 シリカ粉成形体
21 水素ガス供給ノズル
DESCRIPTION OF SYMBOLS 1 Silica glass crucible 2 Transparent silica glass layer 3 Opaque silica glass layer 10 Silica glass crucible manufacturing apparatus 11 Crucible mold 12 Inner member 13 Ventilation part 14 Holding body 15 Rotating shaft 16 Opening part 17 Exhaust port 18 Decompression mechanism 19 Carbon electrode 20 Silica powder molding 21 Hydrogen gas supply nozzle
Claims (2)
酸素雰囲気中でのアーク放電による加熱溶融の際に、シリカ粉成形体の直胴部内表面に沿って水素ガスを供給することを特徴とするシリコン単結晶引上げ用シリカガラスルツボの製造方法。 A production method for obtaining a silica glass crucible by supplying quartz raw material powder into a mold to form a silica powder molded body having a straight body portion, a corner portion and a bottom portion, and heating and melting the silica powder molded body by arc discharge. There,
A method for producing a silica glass crucible for pulling up a silicon single crystal, characterized in that hydrogen gas is supplied along the inner surface of the straight body portion of a silica powder molded body during heating and melting by arc discharge in an oxygen atmosphere.
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