JP6720841B2 - Method for manufacturing semiconductor silicon single crystal - Google Patents

Method for manufacturing semiconductor silicon single crystal Download PDF

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JP6720841B2
JP6720841B2 JP2016223812A JP2016223812A JP6720841B2 JP 6720841 B2 JP6720841 B2 JP 6720841B2 JP 2016223812 A JP2016223812 A JP 2016223812A JP 2016223812 A JP2016223812 A JP 2016223812A JP 6720841 B2 JP6720841 B2 JP 6720841B2
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鈴木 聡
聡 鈴木
義博 児玉
義博 児玉
慶一 中澤
慶一 中澤
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Shin Etsu Handotai Co Ltd
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本発明は、FZ法(フローティングゾーン法または浮遊帯溶融法)による半導体シリコン単結晶(以下、FZシリコン単結晶と言う場合もある)の製造方法に関する。 The present invention relates to a method for producing a semiconductor silicon single crystal (hereinafter, also referred to as FZ silicon single crystal) by the FZ method (floating zone method or floating zone melting method).

FZ法は、例えば、現在半導体素子として最も多く使用されているシリコン単結晶等の半導体単結晶の製造方法の一つとして、使用される。 The FZ method is used, for example, as one of the methods for producing a semiconductor single crystal such as a silicon single crystal which is most often used as a semiconductor element at present.

図9はFZ法によるFZシリコン単結晶の製造方法における各製造工程の一例を説明する概略図である。図9に示すように、原料となる半導体棒(原料棒)104の下端部を溶融して種結晶105に融着させ((a)種付工程)、更にこの種付の際に結晶に生じた転位を抜くための絞り(ネッキング)を行い((b)ネッキング工程)、その後に晶出側半導体棒(半導体単結晶棒)109を所望の直径まで拡大させながら成長させる((c)コーン部形成工程)。更に、晶出側半導体棒109を所望の直径に制御しつつ成長を行い((d)直胴部形成工程)、原料の供給を止め、晶出側半導体棒109の直径を縮小させて該晶出側半導体棒109を原料半導体棒104から切り離す((e)切り離し工程)。以上のような工程を経て、半導体結晶(FZシリコン単結晶)を製造することができる。 FIG. 9 is a schematic view illustrating an example of each manufacturing step in the method for manufacturing an FZ silicon single crystal by the FZ method. As shown in FIG. 9, the lower end portion of the semiconductor rod (raw material rod) 104 as a raw material is melted and fused to the seed crystal 105 ((a) seeding step), and further produced in this seeding. Drawing (necking step) to remove the dislocations ((b) necking step), and thereafter, the crystallization side semiconductor rod (semiconductor single crystal rod) 109 is grown while expanding it to a desired diameter ((c) cone portion). Forming process). Further, the crystallization side semiconductor rod 109 is grown while controlling it to have a desired diameter ((d) straight body portion forming step), the supply of the raw material is stopped, and the diameter of the crystallization side semiconductor rod 109 is reduced to reduce the crystal. The outgoing semiconductor rod 109 is separated from the raw semiconductor rod 104 ((e) separating step). A semiconductor crystal (FZ silicon single crystal) can be manufactured through the above steps.

通常、半導体シリコン単結晶に所望の電気抵抗率を与えるためにはN型或いはP型の不純物ドーピングが必要である。FZ法においては、ドーパントガスを溶融帯域に吹き付けるガスドーピング法が知られている(非特許文献1参照)。 Normally, N-type or P-type impurity doping is required to give a desired electrical resistivity to a semiconductor silicon single crystal. In the FZ method, a gas doping method is known in which a dopant gas is blown to the melting zone (see Non-Patent Document 1).

ドーパントガスとして、例えばN型ドーパントであるP(リン)のドーピングにはPH等が、P型ドーパントであるB(ホウ素)のドーピングにはB等が用いられる。シリコン単結晶の電気抵抗率は、これらN型ドーパントとP型ドーパントの結晶中の濃度差により変化するが、通常の結晶製造においてN型ドーパントのみ、或いはP型ドーパントのみをドーピングする場合には、電気抵抗率はドーパント添加量が増加するにつれて低くなる。 As a dopant gas, for example, PH 3 or the like is used for doping P (phosphorus) that is an N-type dopant, and B 2 H 6 or the like is used for doping B (boron) that is a P-type dopant. The electrical resistivity of a silicon single crystal changes depending on the difference in the concentration of these N-type dopant and P-type dopant in the crystal. However, in the case of doping only an N-type dopant or only a P-type dopant in ordinary crystal production, The electrical resistivity becomes lower as the amount of dopant added increases.

所望の電気抵抗率の半導体シリコン単結晶を得るためには、原料の電気抵抗率と所望の電気抵抗率を基に算出されたドーパント添加量が、適正に保たれる必要がある。供給されるドーパントガスの濃度や流量等を調整することによりドーパント添加量を適正に保ちつつFZ法により単結晶を成長させることで、所望の電気抵抗率を持つ半導体シリコン単結晶を得ることができる。 In order to obtain a semiconductor silicon single crystal having a desired electric resistivity, the dopant addition amount calculated based on the electric resistivity of the raw material and the desired electric resistivity needs to be appropriately maintained. A semiconductor silicon single crystal having a desired electrical resistivity can be obtained by growing a single crystal by the FZ method while adjusting the concentration and the flow rate of the supplied dopant gas while appropriately maintaining the dopant addition amount. ..

FZ法ではシリコン融液は浮遊帯域であり、炉内雰囲気以外には他のいずれの部材とも接触することなく製造されるため、FZ法により製造される半導体シリコン単結晶の不純物濃度は極めて低く高純度であることが特徴である。 In the FZ method, the silicon melt is in the floating zone and is produced without contact with any other member other than the atmosphere in the furnace. Therefore, the impurity concentration of the semiconductor silicon single crystal produced by the FZ method is extremely low and high. It is characterized by its purity.

例えば、石英坩堝を用いて半導体シリコン単結晶を製造するCZ法(チョクラルスキー法)では、シリコン融液と坩堝のSiOとの反応によりSiOが生成されてシリコン融液に酸素が溶け込むため、製造されるCZシリコン単結晶には酸素が混入して高酸素濃度となるが、これに対しFZ法による半導体シリコン単結晶は極めて酸素濃度が低くなる。高純度ポリシリコン棒に比べて酸素濃度が高いCZシリコン結晶棒を原料として使用したFZ法の場合でも、通常はその酸素濃度は可能な限り低いことが求められる。 For example, in the CZ method (Czochralski method) for producing a semiconductor silicon single crystal using a quartz crucible, SiO is generated by the reaction between a silicon melt and SiO 2 in the crucible, and oxygen is dissolved in the silicon melt. Oxygen is mixed into the manufactured CZ silicon single crystal to have a high oxygen concentration, whereas the semiconductor silicon single crystal produced by the FZ method has an extremely low oxygen concentration. Even in the case of the FZ method using a CZ silicon crystal rod having a higher oxygen concentration than a high-purity polysilicon rod as a raw material, the oxygen concentration is usually required to be as low as possible.

一方で、FZ法によるシリコンウェーハにもCZ法によるシリコンウェーハ同様のイントリンシックゲッタリング効果或いはスリップ耐性を付与するために、FZ法による半導体シリコン単結晶製造中にシリコン融液に高純度石英のような酸素供給物を接触もしくは挿入させて、シリコン融液に酸素をドープすることによりCZ法による半導体シリコン単結晶並みの酸素濃度であるFZ法による半導体シリコン単結晶を取得する方法(例えば特許文献1、2、3)や、FZシリコン単結晶の周辺部のみ酸素濃度をCZシリコン単結晶並みにすることで機械的強度を上げる方法(例えば特許文献4)が提案されている。 On the other hand, in order to impart the same intrinsic gettering effect or slip resistance as the silicon wafer by the CZ method to the silicon wafer by the FZ method, the silicon melt is made of high-purity quartz during the production of the semiconductor silicon single crystal by the FZ method. A method for obtaining a semiconductor silicon single crystal by the FZ method, which has an oxygen concentration similar to that of the semiconductor silicon single crystal by the CZ method, by contacting or inserting a different oxygen supply material and doping the silicon melt with oxygen (for example, Patent Document 1). 2, 3) or a method of increasing the mechanical strength by making the oxygen concentration in the peripheral portion of the FZ silicon single crystal to be the same as that of the CZ silicon single crystal (for example, Patent Document 4).

また、特許文献5には、炉内雰囲気の酸素分圧を高圧にすることによりメルトの温度変動を変化させ、酸素濃度バラツキを均一にするという方法が開示されている。また、特許文献6には不純物、例えば酸素を多く含む原料を準備し、取得するFZシリコン単結晶が所望の酸素濃度となるような成長条件に決定し導入量を制御する方法が開示されている。 Further, Patent Document 5 discloses a method of increasing the oxygen partial pressure of the atmosphere in the furnace to change the temperature fluctuation of the melt to make the oxygen concentration variation uniform. Further, Patent Document 6 discloses a method in which a raw material containing a large amount of impurities, for example, oxygen is prepared, growth conditions are determined such that the obtained FZ silicon single crystal has a desired oxygen concentration, and the introduction amount is controlled. ..

特開昭59−102891号公報JP-A-59-102891 特開平02−197118号公報JP-A-02-197118 特許第2807688号公報Japanese Patent No. 2807688 特開平07−291783号公報Japanese Patent Laid-Open No. 07-291783 特開2000−335995号公報JP, 2000-335995, A 特開2015−160800号公報JP, 2005-160800, A

WOLFGANG KELLER、ALFRED MUHLBAUER著「Floating−Zone Silicon」p.82−92、MARCEL DEKKER, INC.発行WOLFGANG KELLER, ALFRED MUHLBAUER, "Floating-Zone Silicon" p. 82-92, MARCEL DEKKER, INC. Issue

近年、省エネルギーの面からパワーデバイスが脚光を浴びているが、サイリスタ、ダイオード、IGBT(Insulated Gate Bipolar Transistor)などで、He照射や電子線照射を行って格子欠陥を導入しキャリアライフタイムを制御する技術を使用したデバイスがある。このようなデバイスの製造に用いられる半導体ウェーハにおいては、その酸素濃度をある程度高くすることで、比較的簡単に所望の格子欠陥量に制御することができる。 In recent years, power devices have been in the spotlight from the viewpoint of energy saving, but thyristors, diodes, IGBTs (Insulated Gate Bipolar Transistors), etc. are used to introduce lattice defects by He irradiation or electron beam irradiation to control carrier lifetime. There are devices that use technology. In a semiconductor wafer used for manufacturing such a device, it is possible to relatively easily control to a desired lattice defect amount by increasing the oxygen concentration to some extent.

このようなスイッチングデバイスに用いられるシリコンウェーハの原料となるFZ法による半導体シリコン単結晶は、高純度ポリシリコン棒或いはCZ法により製造されたCZシリコン結晶棒を原料として製造されるものである。これらの半導体シリコン単結晶の酸素濃度は、高純度ポリシリコン棒を原料とした場合では5.6×1015atoms/cmより小さくなり、またCZシリコン結晶を原料として使用した場合では1.4×1016atoms/cm〜1.9×1016atoms/cmといずれも低いレベルである。一方、CZ法による半導体シリコン単結晶の場合は、その酸素濃度は1.6×1017atoms/cm以上と高いレベルである。デバイス特性を更に高めようとすると、材料であるシリコンウェーハの酸素濃度を、前記のFZ法による半導体シリコン単結晶とCZ法による半導体シリコン単結晶の間のレベルである程度狭い範囲に収めることが望ましく、実質的にはFZ法による半導体シリコン単結晶の酸素濃度を前記で述べた従来のレベルよりも高める必要がある。 A semiconductor silicon single crystal by the FZ method, which is a raw material of a silicon wafer used for such a switching device, is manufactured by using a high-purity polysilicon rod or a CZ silicon crystal rod manufactured by the CZ method as a raw material. The oxygen concentration of these semiconductor silicon single crystals was smaller than 5.6×10 15 atoms/cm 3 when a high-purity polysilicon rod was used as the raw material, and 1.4 when the CZ silicon crystal was used as the raw material. All of them are at a low level of ×10 16 atoms/cm 3 to 1.9×10 16 atoms/cm 3 . On the other hand, in the case of the semiconductor silicon single crystal by the CZ method, the oxygen concentration is as high as 1.6×10 17 atoms/cm 3 or more. In order to further improve the device characteristics, it is desirable that the oxygen concentration of the silicon wafer, which is a material, be kept within a certain narrow range at a level between the semiconductor silicon single crystal by the FZ method and the semiconductor silicon single crystal by the CZ method. Substantially, the oxygen concentration of the semiconductor silicon single crystal by the FZ method needs to be higher than the conventional level described above.

また、FZ法による半導体シリコン単結晶の酸素濃度を高めることについては、CZシリコン単結晶と同等の酸素濃度まで高める目的で製造されることはあっても、所定の範囲に酸素濃度を収めるという目的で製造されることは無かった。 Further, regarding the increase of the oxygen concentration of the semiconductor silicon single crystal by the FZ method, although it is manufactured for the purpose of increasing the oxygen concentration to the same level as that of the CZ silicon single crystal, the purpose is to keep the oxygen concentration within a predetermined range. It was never manufactured in.

そこで、所望の酸素濃度であるFZ法による半導体シリコン単結晶を製造しようとした時に、先行文献の方法はいずれも、酸素濃度の低い半導体シリコン単結晶に対してFZ中に何らかの形で外部から酸素を追加するという手法により行う。この場合、半導体シリコン単結晶の酸素濃度はCZシリコン単結晶並みのかなりの高濃度となる。更に、近年のFZ法による大直径半導体シリコン単結晶製造(例えば200mm)において、このような手法を適用した場合、半導体シリコン単結晶の取得自体が困難になる、酸素濃度以外の品質(例えば面内抵抗率分布)が悪化する、などの不具合が出ることが確実であり、結晶取得可能でより簡単・確実な方法での所望品質のFZ法による半導体シリコン単結晶の製造が望まれている。 Therefore, when an attempt is made to produce a semiconductor silicon single crystal by the FZ method, which has a desired oxygen concentration, all the methods of the prior art documents use some form of external oxygen in the FZ for a semiconductor silicon single crystal having a low oxygen concentration. Is added. In this case, the concentration of oxygen in the semiconductor silicon single crystal is as high as that of CZ silicon single crystal. Furthermore, in the recent large-diameter semiconductor silicon single crystal production (for example, 200 mm) by the FZ method, when such a method is applied, it becomes difficult to obtain the semiconductor silicon single crystal itself. It is certain that problems such as deterioration of resistivity distribution) will occur, and it is desired to manufacture a semiconductor silicon single crystal by the FZ method of desired quality by a simple and reliable method capable of obtaining a crystal.

ここで、半導体シリコン単結晶はその成長方向に直行する断面、すなわちウェーハ面内において酸素濃度が完全に均一ではなく分布を持つものである。更に、原料となるCZシリコン結晶においてもその酸素濃度は結晶全体で均一というわけではなく、成長方向に酸素濃度分布が生じている。このため、製造する半導体シリコン単結晶全体が所望とする酸素濃度範囲に収まるようにするためには断面内及び成長方向の酸素濃度分布を考慮する必要があり、特に要求される酸素濃度範囲が小さくなる場合には、品質不適合な部分が生じてしまう可能性が高くなるため、工夫が必要となる。 Here, the semiconductor silicon single crystal has an oxygen concentration which is not completely uniform but has a distribution in a cross section perpendicular to the growth direction, that is, in the wafer surface. Further, even in the CZ silicon crystal as a raw material, the oxygen concentration is not uniform throughout the crystal, and an oxygen concentration distribution occurs in the growth direction. Therefore, it is necessary to consider the oxygen concentration distribution in the cross section and in the growth direction in order to keep the whole semiconductor silicon single crystal to be produced within the desired oxygen concentration range, and especially the required oxygen concentration range is small. In such a case, there is a high possibility that a quality non-conforming part will occur, so that some ingenuity is required.

また、要求される酸素濃度範囲が、ある程度の変動が許容される程度に広く、品質不適合な部分が生ずることが無くても、同一結晶内の各部分により酸素濃度レベルに差があれば、サーマルドナー発生の程度も変化するなど品質差に繋がり、半導体デバイス製造時の歩留に影響を与える可能性がある。 In addition, the required oxygen concentration range is wide enough to allow some fluctuation, and even if there are no quality-incompatible parts, if there is a difference in oxygen concentration level due to each part in the same crystal, thermal This may lead to quality differences such as changes in the degree of donor generation, which may affect the yield during semiconductor device manufacturing.

本発明はこのような問題に鑑みてなされたものであり、FZ法による半導体シリコン単結晶の製造において、製造する半導体シリコン単結晶全体で酸素濃度が所望とする範囲に収まるような、半導体シリコン単結晶の製造方法を提供することを目的とする。 The present invention has been made in view of the above problems, and in the production of a semiconductor silicon single crystal by the FZ method, a semiconductor silicon single crystal having an oxygen concentration within a desired range in the entire semiconductor silicon single crystal to be produced is provided. An object is to provide a method for producing crystals.

上記目的を達成するために、本発明によれば、CZ法により製造したCZシリコン結晶を原料としたFZ法による半導体シリコン単結晶の製造方法において、
前記CZシリコン結晶の軸方向の酸素濃度を予め測定して酸素濃度分布を取得する工程と、
前記取得したCZシリコン結晶の軸方向の酸素濃度分布に応じて、前記CZシリコン結晶の形状を加工する工程と、
前記形状を加工したCZシリコン結晶を原料として用い、FZ法により前記半導体シリコン単結晶を製造する工程とを有することを特徴とするFZ法による半導体シリコン単結晶の製造方法を提供する。
In order to achieve the above object, according to the present invention, in a method for producing a semiconductor silicon single crystal by the FZ method using a CZ silicon crystal produced by the CZ method as a raw material,
Preliminarily measuring the oxygen concentration in the axial direction of the CZ silicon crystal to obtain an oxygen concentration distribution,
Processing the shape of the CZ silicon crystal according to the obtained oxygen concentration distribution in the axial direction of the CZ silicon crystal;
And a step of producing the semiconductor silicon single crystal by the FZ method, using the CZ silicon crystal having the shape processed as a raw material, the method for producing the semiconductor silicon single crystal by the FZ method.

このように、予め取得したCZシリコン結晶の軸方向の酸素濃度分布に応じて、CZシリコン結晶の形状の加工を行ってから、この形状を加工したCZシリコン結晶を原料として用い、FZ法により半導体シリコン単結晶を製造することにより、製造するFZ半導体シリコン単結晶全体で酸素濃度が所望とする範囲に収まるように制御することができる。 Thus, after the shape of the CZ silicon crystal is processed according to the oxygen concentration distribution in the axial direction of the CZ silicon crystal acquired in advance, the CZ silicon crystal processed in this shape is used as a raw material and the semiconductor is processed by the FZ method. By producing a silicon single crystal, it is possible to control the oxygen concentration of the produced FZ semiconductor silicon single crystal so that it falls within a desired range.

このとき、前記CZシリコン結晶の形状を加工する工程において、
前記取得したCZシリコン結晶の軸方向の酸素濃度分布に相関するように、前記CZシリコン結晶の直径を軸方向で変化させるように加工することが好ましい。
At this time, in the step of processing the shape of the CZ silicon crystal,
It is preferable that the diameter of the CZ silicon crystal is changed in the axial direction so as to correlate with the obtained oxygen concentration distribution of the CZ silicon crystal in the axial direction.

このようにすれば、製造する半導体シリコン単結晶全体で酸素濃度が所望とする範囲に収まるように効果的に制御することができる。 By doing so, it is possible to effectively control the oxygen concentration within the desired range in the entire semiconductor silicon single crystal to be manufactured.

またこのとき、前記CZシリコン結晶の形状を加工する工程において、
前記取得したCZシリコン結晶の軸方向の酸素濃度分布における、前記酸素濃度が高い位置の前記CZシリコン結晶の直径に比べて、前記酸素濃度が低い位置の前記CZシリコン結晶の直径が小さくなるように加工することが好ましい。
At this time, in the step of processing the shape of the CZ silicon crystal,
In the axial oxygen concentration distribution of the obtained CZ silicon crystal, the diameter of the CZ silicon crystal at the low oxygen concentration position is smaller than the diameter of the CZ silicon crystal at the high oxygen concentration position. It is preferably processed.

このように、取得したCZシリコン結晶の軸方向の酸素濃度分布における、酸素濃度の大小に合わせて、それを打ち消すように原料直径を変化させるような加工を行ってから結晶製造することにより、FZ法による半導体シリコン単結晶の酸素濃度を成長方向で均一に近づけて、結晶全体で所望の酸素濃度範囲に制御することがより確実にできる。 In this way, by performing processing such that the raw material diameter is changed so as to cancel out the oxygen concentration in the obtained oxygen concentration distribution in the axial direction of the CZ silicon crystal according to the magnitude of the oxygen concentration, the FZ is manufactured. It is possible to make the oxygen concentration of the semiconductor silicon single crystal closer to a uniform value in the growth direction by the method, and more reliably control the oxygen concentration in the desired range over the entire crystal.

またこのとき、前記FZ法で製造する半導体シリコン単結晶の直径を150mm以上とすることが好ましい。 At this time, the diameter of the semiconductor silicon single crystal produced by the FZ method is preferably 150 mm or more.

このような大直径単結晶の製造においても、本発明では確実に単結晶を取得することが可能となる。 Even in the production of such a large diameter single crystal, the present invention makes it possible to reliably obtain the single crystal.

またこのとき、所望とする前記FZ法で製造する半導体シリコン単結晶の酸素濃度の50倍以上の酸素濃度を有する前記CZシリコン結晶を原料として用いることが好ましい。 At this time, it is preferable to use, as a raw material, the CZ silicon crystal having an oxygen concentration of 50 times or more the desired oxygen concentration of the semiconductor silicon single crystal produced by the FZ method.

このようにすれば、高品質なFZ単結晶を取得するための製造条件で、所望とする酸素濃度範囲の半導体シリコン結晶を得ることができ、FZ法の製造条件を大幅に変更するような制約を設けることがない。 By doing so, it is possible to obtain a semiconductor silicon crystal having a desired oxygen concentration range under the manufacturing conditions for obtaining a high-quality FZ single crystal, and it is necessary to significantly change the manufacturing conditions of the FZ method. Is not provided.

またこのとき、前記FZ法で製造する半導体シリコン単結晶の軸方向の全体で、酸素濃度が2.1×1016atoms/cm以上8.0×1016atoms/cm以下、より好ましくは、4.0×1016atoms/cm以上5.0×1016atoms/cm以下の範囲であることが好ましい。なお、本発明において用いる酸素濃度は、ASTM’79に基づくものである。 At this time, the oxygen concentration of the entire semiconductor silicon single crystal produced by the FZ method in the axial direction is 2.1×10 16 atoms/cm 3 or more and 8.0×10 16 atoms/cm 3 or less, and more preferably It is preferably in the range of 4.0×10 16 atoms/cm 3 or more and 5.0×10 16 atoms/cm 3 or less. The oxygen concentration used in the present invention is based on ASTM'79.

このようにすれば、FZ法で製造する半導体シリコン単結晶の軸方向の全体で酸素濃度が、従来のFZ法による半導体シリコン単結晶より高いレベルで、かつ所定の狭い範囲内に収まる半導体シリコン単結晶を製造することができる。 With this configuration, the oxygen concentration in the entire axial direction of the semiconductor silicon single crystal produced by the FZ method is higher than that of the semiconductor silicon single crystal produced by the conventional FZ method, and the semiconductor silicon single crystal is within a predetermined narrow range. Crystals can be produced.

本発明の半導体シリコン単結晶の製造方法であれば、予め取得したCZシリコン結晶の軸方向の酸素濃度分布に応じて、CZシリコン結晶の形状の加工を行ってから、この形状を加工したCZシリコン結晶を原料として用い、FZ法により半導体シリコン単結晶を製造することにより、製造する半導体シリコン単結晶全体で酸素濃度が所望とする範囲に収まるように制御することができる。これにより半導体シリコン単結晶全体においてデバイス製造時に要求される品質を満たすことができるため、当該結晶の品質および生産性が向上するとともに、安定するため、製品の安定供給が可能となる。 According to the method for producing a semiconductor silicon single crystal of the present invention, the shape of the CZ silicon crystal is processed according to the oxygen concentration distribution in the axial direction of the CZ silicon crystal acquired in advance, and then the CZ silicon processed by this shape is processed. By using a crystal as a raw material and manufacturing a semiconductor silicon single crystal by the FZ method, it is possible to control the oxygen concentration of the entire manufactured semiconductor silicon single crystal to fall within a desired range. As a result, the quality required for manufacturing the device can be satisfied in the entire semiconductor silicon single crystal, and the quality and productivity of the crystal are improved, and the crystal is stable, so that a stable product supply can be achieved.

本発明の半導体シリコン単結晶の製造方法の一例を示した工程図である。FIG. 3 is a process chart showing an example of a method for producing a semiconductor silicon single crystal of the present invention. 本発明の半導体シリコン単結晶の製造方法に用いられる半導体単結晶の製造装置を示す概略図である。It is a schematic diagram showing a manufacturing device of a semiconductor single crystal used for a manufacturing method of a semiconductor silicon single crystal of the present invention. 半導体シリコン単結晶の断面内の酸素濃度分布の一例を示すグラフである。It is a graph which shows an example of oxygen concentration distribution in the cross section of semiconductor silicon single crystal. CZシリコン原料結晶の軸方向の酸素濃度分布の一例を示すグラフである。It is a graph which shows an example of the oxygen concentration distribution of the CZ silicon raw material crystal in the axial direction. 不純物導入率(FZ結晶中酸素濃度/原料中酸素濃度)と数値Kとの関係を表すグラフである。6 is a graph showing a relationship between an impurity introduction rate (oxygen concentration in FZ crystal/oxygen concentration in raw material) and a numerical value K. 実施例において加工を行ったCZシリコン原料結晶の直径を示したグラフである。It is the graph which showed the diameter of the CZ silicon raw material crystal processed in the Example. 実施例において製造したFZシリコン単結晶の軸方向の酸素濃度分布を示したグラフである。It is the graph which showed the oxygen concentration distribution of the axial direction of the FZ silicon single crystal manufactured in the Example. 比較例において製造したFZシリコン単結晶の軸方向の酸素濃度分布を示したグラフである。It is the graph which showed the oxygen concentration distribution of the axial direction of the FZ silicon single crystal manufactured in the comparative example. FZ法による半導体単結晶の製造方法における各製造工程の一例を説明する概略図である。It is a schematic diagram explaining an example of each manufacturing process in a manufacturing method of a semiconductor single crystal by the FZ method.

以下、本発明について実施の形態を説明するが、本発明はこれに限定されるものではない。 Hereinafter, embodiments of the present invention will be described, but the present invention is not limited thereto.

前述のように、従来、FZ法による半導体シリコン単結晶に求められる品質としては高純度化、すなわちできるだけ不純物濃度は低くすることが望ましく、またそれがFZ法による半導体シリコン単結晶の特徴の一つでもあった。 As described above, it is desirable that the quality conventionally required for the semiconductor silicon single crystal by the FZ method is high purification, that is, the impurity concentration is as low as possible, which is one of the characteristics of the semiconductor silicon single crystal by the FZ method. It was also.

しかしながら、FZ法による半導体シリコンウェーハから製造されるデバイスの製造方法によっては、ある程度の不純物、例えば酸素が半導体シリコン単結晶に一定量含有していた方が好ましい場合があり、本発明者らは前記のような問題に対処すべく鋭意・検討を行った。その結果、予め取得したCZシリコン結晶の軸方向の酸素濃度分布に応じて、CZシリコン結晶の形状の加工を行ってから、この形状を加工したCZシリコン結晶を原料として用い、FZ法により半導体シリコン単結晶を製造することにより、製造する半導体シリコン単結晶全体で酸素濃度が所望とする範囲に収まるように制御することができることを見出した。そして、これらを実施するための最良の形態について精査し、本発明を完成させた。 However, depending on the method of manufacturing a device manufactured from a semiconductor silicon wafer by the FZ method, it may be preferable that a certain amount of impurities such as oxygen be contained in the semiconductor silicon single crystal in a certain amount. We conducted a thorough study to deal with such problems. As a result, the CZ silicon crystal shape is processed in accordance with the axial oxygen concentration distribution of the CZ silicon crystal acquired in advance, and the CZ silicon crystal processed in this shape is used as a raw material. It has been found that by producing a single crystal, the oxygen concentration of the entire semiconductor silicon single crystal produced can be controlled so as to fall within a desired range. Then, the best mode for carrying out these was scrutinized to complete the present invention.

まず、本発明の半導体シリコン単結晶の製造を行うことができる半導体シリコン単結晶製造装置の一例について、図2を参照して説明する。 First, an example of a semiconductor silicon single crystal production apparatus capable of producing a semiconductor silicon single crystal of the present invention will be described with reference to FIG.

図2に示すように、半導体シリコン単結晶製造装置10のチャンバー11内には上軸12及び下軸13が設けられている。上軸12には原料半導体棒(CZシリコン結晶14)として所定の直径のCZシリコン結晶14が、下軸13には種結晶15が取り付けられるようになっている。 As shown in FIG. 2, an upper shaft 12 and a lower shaft 13 are provided in the chamber 11 of the semiconductor silicon single crystal manufacturing apparatus 10. A CZ silicon crystal 14 having a predetermined diameter is attached to the upper shaft 12 as a raw material semiconductor rod (CZ silicon crystal 14), and a seed crystal 15 is attached to the lower shaft 13.

さらに、CZシリコン結晶14を溶融する高周波加熱コイル16を備え、溶融帯域18をCZシリコン結晶14に対して相対的に移動させながら晶出半導体棒(半導体シリコン単結晶19)を成長させることができる。また、成長中に、ドープノズル20(ドーパントガス供給手段)からドーパントガスを供給できるようになっている。 Further, the high frequency heating coil 16 for melting the CZ silicon crystal 14 is provided, and the crystallized semiconductor rod (semiconductor silicon single crystal 19) can be grown while moving the melting zone 18 relative to the CZ silicon crystal 14. .. Further, the dopant gas can be supplied from the dope nozzle 20 (dopant gas supply means) during the growth.

次に、本発明の半導体シリコン単結晶の製造方法について図1を参照して説明する。以下では、上記した図2の半導体シリコン単結晶製造装置を用いる場合について説明する。 Next, a method for manufacturing a semiconductor silicon single crystal of the present invention will be described with reference to FIG. Hereinafter, a case where the semiconductor silicon single crystal manufacturing apparatus of FIG. 2 described above is used will be described.

まず、原料として、CZ法により製造したCZシリコン単結晶を準備する。そして、CZシリコン結晶の軸方向の酸素濃度を予め測定して酸素濃度分布を取得する工程を行う(図1のSP1)。 First, a CZ silicon single crystal manufactured by the CZ method is prepared as a raw material. Then, a step of measuring the oxygen concentration in the axial direction of the CZ silicon crystal in advance and acquiring the oxygen concentration distribution is performed (SP1 in FIG. 1).

ここで、所望とするFZ法で製造する半導体シリコン単結晶の酸素濃度の50倍以上の酸素濃度を有するCZシリコン結晶を原料として用いることが好ましい。このようにすれば、例え、FZ中に酸素が飛散して低酸素となったとしても、高品質なFZ単結晶を取得するための製造条件で、所望とする酸素濃度範囲の半導体シリコン結晶を得ることができ、製造条件を大幅に変更するような制約を設けることがない。 Here, it is preferable to use, as a raw material, a CZ silicon crystal having an oxygen concentration of 50 times or more the oxygen concentration of a desired semiconductor silicon single crystal produced by the FZ method. By doing so, even if oxygen is scattered into FZ and becomes low oxygen, a semiconductor silicon crystal having a desired oxygen concentration range can be obtained under the manufacturing conditions for obtaining a high-quality FZ single crystal. It can be obtained, and there is no restriction that drastically changes the manufacturing conditions.

またこのとき、上記所望とする酸素濃度は、FZ法で製造する半導体シリコン単結晶の軸方向の全体で、酸素濃度が2.1×1016atoms/cm以上8.0×1016atoms/cm以下、より好ましくは、4.0×1016atoms/cm以上5.0×1016atoms/cm以下の範囲であることが好ましい。なお、本発明において用いる酸素濃度は、ASTM’79に基づくものである。 At this time, the desired oxygen concentration is 2.1×10 16 atoms/cm 3 or more and 8.0×10 16 atoms/cm 3 or more in the entire axial direction of the semiconductor silicon single crystal produced by the FZ method. cm 3 or less, more preferably 4.0×10 16 atoms/cm 3 or more and 5.0×10 16 atoms/cm 3 or less. The oxygen concentration used in the present invention is based on ASTM'79.

このように、FZ法で製造する半導体シリコン単結晶の軸方向の全体で酸素濃度が、従来のFZ法による半導体シリコン単結晶より高いレベルで、かつ所定の狭い範囲内に収まる半導体シリコン単結晶を製造することができる。 Thus, the semiconductor silicon single crystal produced by the FZ method has a higher oxygen concentration in the entire axial direction than that of the conventional semiconductor silicon single crystal by the FZ method, and the semiconductor silicon single crystal is contained within a predetermined narrow range. It can be manufactured.

次に、取得したCZシリコン結晶の軸方向の酸素濃度分布に応じて、前記CZシリコン結晶の形状を加工する工程を行う(図1のSP2)。 Next, a step of processing the shape of the CZ silicon crystal is performed according to the obtained oxygen concentration distribution of the CZ silicon crystal in the axial direction (SP2 in FIG. 1).

ここで、取得したCZシリコン結晶の軸方向の酸素濃度分布に相関するように、CZシリコン結晶の直径を軸方向で変化させるように加工することが好ましい。このようにすれば、製造するFZ半導体シリコン単結晶全体で酸素濃度が所望とする範囲に収まるように効果的に制御することができる。 Here, it is preferable to perform processing so that the diameter of the CZ silicon crystal is changed in the axial direction so as to correlate with the obtained oxygen concentration distribution of the CZ silicon crystal in the axial direction. By doing so, it is possible to effectively control the oxygen concentration in the entire FZ semiconductor silicon single crystal to be manufactured so as to fall within a desired range.

以下に原料結晶(CZシリコン結晶)の直径を調整することで、FZ法で製造する半導体シリコン単結晶の軸方向の酸素濃度分布を改善できることについて説明する。 It will be described below that the oxygen concentration distribution in the axial direction of the semiconductor silicon single crystal produced by the FZ method can be improved by adjusting the diameter of the raw material crystal (CZ silicon crystal).

FZ法により製造する半導体シリコン単結晶に導入される酸素は、CZ原料中の含有酸素がメルト(図2中の溶融帯域18)に供給され、メルトから蒸発する分を除いた量がFZ単結晶に導入されるものと考えられ、実際に単結晶に導入される酸素量を決定するのはその時々のメルト内酸素濃度、特に凝固界面近傍の酸素濃度であると考えられる。メルト中の酸素は炉内雰囲気と接するメルト表面から蒸発するため、メルト表面近傍ではメルト内酸素濃度は低くなる。このため結晶直径方向での凝固界面近傍のメルト内酸素濃度分布は、メルト表面に近い結晶外周側は低くなり、結晶中央は高くなる。よって、製造された半導体シリコン単結晶の断面方向の酸素濃度も一様にはならず、メルト内酸素濃度分布と同様の傾向となる。図3に半導体シリコン単結晶の断面内酸素濃度分布の一例を示す。 Regarding the oxygen introduced into the semiconductor silicon single crystal produced by the FZ method, the oxygen contained in the CZ raw material is supplied to the melt (melting zone 18 in FIG. 2), and the amount removed from the melt is the FZ single crystal. It is thought that the oxygen amount actually introduced into the single crystal determines the oxygen concentration in the melt at that time, particularly the oxygen concentration near the solidification interface. Since oxygen in the melt evaporates from the melt surface in contact with the atmosphere in the furnace, the oxygen concentration in the melt becomes low near the melt surface. Therefore, the oxygen concentration distribution in the melt in the vicinity of the solidification interface in the crystal diameter direction is low on the crystal outer peripheral side close to the melt surface and high in the crystal center. Therefore, the oxygen concentration in the cross-sectional direction of the manufactured semiconductor silicon single crystal is not uniform and has the same tendency as the oxygen concentration distribution in the melt. FIG. 3 shows an example of the oxygen concentration distribution in the cross section of the semiconductor silicon single crystal.

更に、メルトに供給される酸素はCZ原料中の含有酸素であるため、FZ法により半導体シリコン単結晶成長中の各時点で溶融する原料の酸素濃度によって供給される酸素量は変化する。すなわち、原料として使用するCZシリコン結晶の長手方向(軸方向)の酸素濃度変化が、FZ法で製造する半導体シリコン単結晶の成長方向(軸方向)の酸素濃度変化に影響する。 Furthermore, since the oxygen supplied to the melt is the oxygen contained in the CZ raw material, the amount of oxygen supplied changes depending on the oxygen concentration of the raw material melted at each time point during the semiconductor silicon single crystal growth by the FZ method. That is, the change in oxygen concentration in the longitudinal direction (axial direction) of the CZ silicon crystal used as a raw material affects the change in oxygen concentration in the growth direction (axial direction) of the semiconductor silicon single crystal produced by the FZ method.

前記のように、製造する半導体シリコン単結晶全体で考えた場合、結晶のどの部分でもその酸素濃度が完全に均一とは言い難く、断面内及び結晶成長方向の酸素濃度の変化によりある程度の酸素濃度範囲を持つことになる。このため、結晶全体を所望の酸素濃度範囲に収める場合、断面内の酸素濃度変化及び/又は結晶成長方向の酸素濃度変化を小さくする必要がある。 As described above, when considering the entire semiconductor silicon single crystal to be manufactured, it is difficult to say that the oxygen concentration is completely uniform in any part of the crystal. Will have a range. For this reason, when the entire crystal is kept in a desired oxygen concentration range, it is necessary to reduce the change in oxygen concentration in the cross section and/or the change in oxygen concentration in the crystal growth direction.

しかしながら、半導体シリコン単結晶断面内の酸素濃度変化を均一にすることはその成長原理上難しく、結晶が断面内酸素濃度分布を持つことは避けられないと考えられる。このため、結晶成長方向の酸素濃度変動を抑える必要があるが、そのための一つの方法として原料長手方向の酸素濃度変動を抑えることが考えられる。ところが、特に従来のレベルよりも高い酸素濃度となる半導体シリコン単結晶を取得しようとする時には原料となるCZシリコン結晶もより高酸素濃度にする必要があり、このような場合、CZシリコン結晶の長手方向の酸素濃度変化を抑えることも難しい。 However, it is difficult to make the oxygen concentration change in the cross section of the semiconductor silicon single crystal uniform due to its growth principle, and it is inevitable that the crystal has the oxygen concentration distribution in the cross section. Therefore, it is necessary to suppress the fluctuation of oxygen concentration in the crystal growth direction, but one method for achieving this is to suppress the fluctuation of oxygen concentration in the longitudinal direction of the raw material. However, particularly when obtaining a semiconductor silicon single crystal having an oxygen concentration higher than the conventional level, it is necessary to increase the oxygen concentration of the CZ silicon crystal as a raw material. In such a case, the longitudinal length of the CZ silicon crystal is increased. It is also difficult to suppress the change in oxygen concentration in the direction.

よって、原料となるCZシリコン結晶の長手方向の酸素濃度の変化も避けられないものとして、原料中の酸素濃度変化に応じて原料直径を調整することで、前記原料を用いて半導体シリコン単結晶成長させて取得するFZ法による半導体シリコン単結晶の酸素濃度を軸方向の全体で、所望の範囲内に収めることを実現する。 Therefore, assuming that the change in the oxygen concentration in the longitudinal direction of the CZ silicon crystal as the raw material is unavoidable, the diameter of the raw material is adjusted according to the change in the oxygen concentration in the raw material to grow a semiconductor silicon single crystal using the raw material. Thus, the oxygen concentration of the semiconductor silicon single crystal obtained by the FZ method can be kept within a desired range in the entire axial direction.

そこで、上記したように、予め原料となるCZシリコン結晶の酸素濃度を測定し(SP1)、長手方向の変化を確認しておく。図4に原料長手方向の酸素濃度分布の一例を示す。例えば図4のような酸素濃度分布を持つ原料を用いた場合、半導体シリコン単結晶の成長とともにメルトに供給される酸素量が減少するため、通常では、取得するFZ半導体シリコン単結晶の酸素濃度は成長初期の方が高く、終盤の方が低くなる。すなわち、半導体シリコン単結晶の成長方向酸素濃度分布はCZ原料長手方向酸素濃度分布の傾向と同様となる。 Therefore, as described above, the oxygen concentration of the CZ silicon crystal that is the raw material is measured in advance (SP1), and the change in the longitudinal direction is confirmed. FIG. 4 shows an example of the oxygen concentration distribution in the longitudinal direction of the raw material. For example, when a raw material having an oxygen concentration distribution as shown in FIG. 4 is used, the amount of oxygen supplied to the melt decreases as the semiconductor silicon single crystal grows. Higher at the beginning of growth and lower at the end of growth. That is, the oxygen concentration distribution in the growth direction of the semiconductor silicon single crystal has the same tendency as the oxygen concentration distribution in the longitudinal direction of the CZ raw material.

ここで、実際に半導体シリコン単結晶に導入される酸素量は、蒸発により大半は除去されてしまうためにメルトに供給される酸素量よりも少なくなる。 Here, the amount of oxygen actually introduced into the semiconductor silicon single crystal is less than the amount of oxygen supplied to the melt because most of it is removed by evaporation.

半導体シリコン単結晶成長中のメルトからの酸素蒸発量は、メルト滞留時間、メルト表面積と比例し、炉内圧力と相反する関係にある。よって、原料酸素濃度を分母とし、FZシリコン単結晶酸素濃度を分子とした酸素導入率は、(メルト滞留時間)×(メルト表面積)/(炉内圧力)で表わされる数値Kにより決定される。 The amount of oxygen evaporated from the melt during the growth of the semiconductor silicon single crystal is proportional to the melt residence time and the melt surface area, and has a contradictory relationship with the furnace pressure. Therefore, the oxygen introduction rate with the raw material oxygen concentration as the denominator and the FZ silicon single crystal oxygen concentration as the numerator is determined by the numerical value K represented by (melt retention time)×(melt surface area)/(furnace pressure).

ここで、メルト滞留時間の要素は直胴時の溶融メルト量と結晶単位時間内の原料溶融量(結晶成長量)すなわち結晶成長速度が関わるものであるが、厳密には原料直径が一定であることによる原料供給速度が一定という条件下で成り立つものであり、原料直径が変化する場合には原料が溶融して成長単結晶の上に滞留するメルト内に落ち込むまでの酸素の蒸発量の変化も存在すると考えられる。 Here, the element of the melt residence time is related to the amount of melted melt in a straight body and the amount of melted raw material within a crystal unit time (crystal growth amount), that is, the crystal growth rate, but strictly speaking, the raw material diameter is constant. This is true under the condition that the raw material supply rate is constant, and when the raw material diameter changes, the change in the evaporation amount of oxygen until the raw material melts and falls into the melt staying on the growing single crystal. It is thought to exist.

すなわち、原料供給速度のパラメータが酸素濃度に影響すると考えられ、単位時間当たりの結晶成長量の関係から、((結晶直径)/(原料直径))×(結晶成長速度)と算出される原料供給速度の操作により酸素導入率を変化させることができる。 That is, it is considered that the parameter of the raw material supply rate influences the oxygen concentration, and from the relationship of the crystal growth amount per unit time, the raw material calculated as ((crystal diameter)/(raw material diameter)) 2 ×(crystal growth rate) The oxygen introduction rate can be changed by controlling the supply rate.

図5は半導体シリコン単結晶製造における数値Kと、原料結晶と半導体シリコン単結晶の酸素濃度比との関係を示す。メルト滞留時間は直胴時の溶融メルト量と結晶単位時間内の原料溶融量(結晶成長量)から算出し、メルト表面積は製造結晶断面積を近似的に用いた。 FIG. 5 shows the relationship between the numerical value K in the production of a semiconductor silicon single crystal and the oxygen concentration ratio between the raw material crystal and the semiconductor silicon single crystal. The melt residence time was calculated from the amount of melted melt in a straight body and the amount of melted raw material (crystal growth amount) within a crystal unit time, and the melt surface area was approximately used as the cross-sectional area of the produced crystal.

予め測定しておいた原料酸素濃度変化、すなわちFZ結晶成長各時点の供給酸素濃度変化と数値Kにより、取得する半導体シリコン単結晶の成長方向の酸素濃度変化範囲が推定できる。 The oxygen concentration change range in the growth direction of the semiconductor silicon single crystal to be acquired can be estimated by the change in the source oxygen concentration measured in advance, that is, the change in the supply oxygen concentration at each time point of the FZ crystal growth and the numerical value K.

この時に結晶成長方向での酸素濃度変化を抑えるために、原料のCZシリコン結晶の直径を長手方向(軸方向)で変化させることで、原料供給速度の変化により、原料からの供給酸素量変化を相殺するような操作を行う。 At this time, in order to suppress the change in oxygen concentration in the crystal growth direction, the diameter of the CZ silicon crystal of the raw material is changed in the longitudinal direction (axial direction). Perform an offsetting operation.

すなわち、予め取得したCZシリコン結晶の軸方向の酸素濃度の増減に対して相関の形で、原料直径を長手方向に変化させるような加工を施してから、FZ法による半導体シリコン単結晶製造に用いることにより、FZ法により製造された半導体シリコン単結晶の成長方向の酸素濃度変動を低減し、結晶全体の酸素濃度変化を断面内の酸素濃度変化の範囲までに抑えることができる。 That is, the CZ silicon crystal is processed in advance in such a manner that the raw material diameter is changed in the longitudinal direction in a manner that correlates with an increase or decrease in the oxygen concentration in the axial direction of the CZ silicon crystal, and then used for manufacturing a semiconductor silicon single crystal by the FZ method. As a result, the variation in oxygen concentration in the growth direction of the semiconductor silicon single crystal manufactured by the FZ method can be reduced, and the variation in oxygen concentration in the entire crystal can be suppressed to the range of variation in oxygen concentration in the cross section.

具体的には、取得したCZシリコン結晶の軸方向の酸素濃度分布における、酸素濃度が高い位置のCZシリコン結晶の直径に比べて、酸素濃度が低い位置のCZシリコン結晶の直径が小さくなるように加工することが好ましい。このように、取得したCZシリコン結晶の軸方向の酸素濃度分布における、酸素濃度の大小に合わせて、それを打ち消すように原料直径を変化させるような加工を行ってからFZ法による結晶製造をすることにより、FZ法による半導体シリコン単結晶の酸素濃度を成長方向で均一に近づけて、結晶全体で所望の酸素濃度範囲に制御することがより確実にできる。この場合、CZシリコン結晶の直径の加工は、外周研削等により簡単に行うことができる。加工後、エッチングや洗浄を行うことにより、FZ法に用いる原料とすることができる。 Specifically, in the obtained oxygen concentration distribution in the axial direction of the CZ silicon crystal, the diameter of the CZ silicon crystal at the low oxygen concentration position is made smaller than the diameter of the CZ silicon crystal at the high oxygen concentration position. It is preferably processed. In this way, according to the oxygen concentration distribution in the axial direction of the obtained CZ silicon crystal, the diameter of the raw material is changed so as to cancel it according to the magnitude of the oxygen concentration, and then the crystal is manufactured by the FZ method. As a result, the oxygen concentration of the semiconductor silicon single crystal obtained by the FZ method can be made closer to uniform in the growth direction, and it can be more surely controlled within the desired oxygen concentration range in the entire crystal. In this case, the diameter of the CZ silicon crystal can be easily processed by grinding the outer circumference. After processing, it can be used as a raw material for the FZ method by performing etching or cleaning.

そして、上記のように形状を加工したCZシリコン結晶を原料として用い、FZ法により半導体シリコン単結晶を製造する工程を行う(図1のSP3)。 Then, a step of manufacturing a semiconductor silicon single crystal by the FZ method is performed using the CZ silicon crystal whose shape is processed as described above as a raw material (SP3 in FIG. 1).

このとき、FZ法で製造する半導体シリコン単結晶の直径を150mm以上とすることが好ましい。本発明では、このような大直径結晶の製造においても確実に所望の酸素濃度範囲の単結晶を取得することが可能となる。 At this time, the diameter of the semiconductor silicon single crystal produced by the FZ method is preferably 150 mm or more. According to the present invention, it is possible to reliably obtain a single crystal having a desired oxygen concentration range even in the production of such a large diameter crystal.

まず、上軸12には原料半導体棒として、上記のように予め軸方向の酸素濃度を測定し、軸方向の酸素濃度分布に応じて形状を加工したCZシリコン結晶14を取り付ける。また、下軸13には種結晶15を取り付ける。 First, as the raw material semiconductor rod, the CZ silicon crystal 14 whose oxygen concentration in the axial direction has been measured in advance and whose shape has been processed according to the oxygen concentration distribution in the axial direction is attached to the upper shaft 12. A seed crystal 15 is attached to the lower shaft 13.

そして、CZシリコン結晶14を高周波加熱コイル16等で溶融した後、種結晶15に融着させる。種結晶から成長させる晶出側半導体棒(半導体シリコン単結晶19)を絞り17により無転位化し、両軸を回転させながら高周波加熱コイル16に対して相対的に下降させ、溶融帯域18をCZシリコン結晶14に対して相対的に上へと移動させながら半導体シリコン単結晶19を成長させる。 Then, the CZ silicon crystal 14 is melted by the high frequency heating coil 16 or the like, and then fused to the seed crystal 15. The crystallization side semiconductor rod (semiconductor silicon single crystal 19) grown from the seed crystal is made dislocation-free by the diaphragm 17 and lowered relative to the high frequency heating coil 16 while rotating both axes, and the melting zone 18 is made of CZ silicon. The semiconductor silicon single crystal 19 is grown while moving upward relative to the crystal 14.

絞り17を形成した後、種結晶15から成長させる半導体シリコン単結晶19を所望の直径まで拡径させながら成長させてコーン部22を形成し、CZシリコン結晶14と半導体シリコン単結晶19との間に溶融帯域18を形成して、原料結晶の直径に応じて上軸の下降速度を調整しつつ、半導体シリコン単結晶19を所望の直径に制御しながら成長させて直胴部21を形成する。 After forming the diaphragm 17, the semiconductor silicon single crystal 19 grown from the seed crystal 15 is grown while being expanded to a desired diameter to form the cone portion 22, and the cone portion 22 is formed, and between the CZ silicon crystal 14 and the semiconductor silicon single crystal 19. A melting zone 18 is formed in the substrate, and the straight body portion 21 is formed by growing the semiconductor silicon single crystal 19 while controlling it to have a desired diameter while adjusting the descending speed of the upper axis according to the diameter of the raw material crystal.

このとき、大幅に製造条件を変更することなく、ほとんど従来通りの製造条件で半導体シリコン単結晶製造を行うことが可能で、半導体シリコン単結晶の生産性を損なうことなく所望の品質を得ることができる。 At this time, the semiconductor silicon single crystal can be manufactured under almost the same manufacturing conditions as the conventional manufacturing conditions without significantly changing the manufacturing conditions, and desired quality can be obtained without impairing the productivity of the semiconductor silicon single crystal. it can.

そして、溶融帯域18をCZシリコン結晶14の上端まで移動させて半導体シリコン単結晶19の直胴部21の成長を終え、半導体シリコン単結晶19の直径を縮径させて該半導体シリコン単結晶19をCZシリコン結晶14から切り離して、半導体シリコン単結晶の製造を終了する。 Then, the melting zone 18 is moved to the upper end of the CZ silicon crystal 14 to complete the growth of the straight body portion 21 of the semiconductor silicon single crystal 19, and the diameter of the semiconductor silicon single crystal 19 is reduced to form the semiconductor silicon single crystal 19. The production of the semiconductor silicon single crystal is completed by separating from the CZ silicon crystal 14.

このような本発明の半導体シリコン単結晶の製造方法であれば、予め取得したCZシリコン結晶の軸方向の酸素濃度分布に応じて、CZシリコン結晶の形状の加工を行ってから、この形状を加工したCZシリコン結晶を原料として用い、FZ法により半導体シリコン単結晶を製造することにより、製造する半導体シリコン単結晶全体で酸素濃度が所望とする範囲に収まるように制御することができる。これにより半導体シリコン単結晶全体においてデバイス製造時に要求される品質を満たすことができるため、当該結晶の生産性が向上、かつ安定し製品の安定供給が可能となる。 According to the method for producing a semiconductor silicon single crystal of the present invention as described above, the shape of the CZ silicon crystal is processed after the shape of the CZ silicon crystal is processed according to the oxygen concentration distribution in the axial direction of the CZ silicon crystal acquired in advance. By using the prepared CZ silicon crystal as a raw material to produce a semiconductor silicon single crystal by the FZ method, it is possible to control the oxygen concentration of the entire semiconductor silicon single crystal produced to fall within a desired range. As a result, the quality required for manufacturing the device can be satisfied in the entire semiconductor silicon single crystal, so that the productivity of the crystal can be improved and the product can be stably supplied in a stable manner.

また、CZシリコン結晶を原料として用いたFZ法による半導体シリコン単結晶の製造方法において、製造された半導体シリコン単結晶断面における酸素濃度分布を考慮しても、結晶全体で所定の酸素濃度範囲となる半導体シリコン単結晶を製造することができる。例えば、FZ法で製造する半導体シリコン単結晶の軸方向の全体で、酸素濃度が2.1×1016atoms/cm以上8.0×1016atoms/cm以下、より好ましくは、4.0×1016atoms/cm以上5.0×1016atoms/cm以下の範囲にすることができる。 Further, in the method of manufacturing a semiconductor silicon single crystal by the FZ method using CZ silicon crystal as a raw material, even if the oxygen concentration distribution in the manufactured semiconductor silicon single crystal cross section is taken into consideration, the entire crystal has a predetermined oxygen concentration range. A semiconductor silicon single crystal can be manufactured. For example, in the entire axial direction of the semiconductor silicon single crystal produced by the FZ method, the oxygen concentration is 2.1×10 16 atoms/cm 3 or more and 8.0×10 16 atoms/cm 3 or less, and more preferably 4. It can be in the range of 0×10 16 atoms/cm 3 or more and 5.0×10 16 atoms/cm 3 or less.

更に、原料結晶の直径に応じて上軸の下降速度を調整すること以外は、単結晶側の成長条件には何ら変更を加える必要がないために、結晶断面内抵抗率分布などのその他の結晶品質が変化することなく前記のような半導体シリコン単結晶を製造することができる。そのため、半導体シリコン単結晶の生産性を損なうことなく所望の品質を得ることができる。 Furthermore, except for adjusting the descending speed of the upper axis according to the diameter of the raw material crystal, there is no need to make any changes to the growth conditions on the single crystal side, so that other crystals such as the resistivity distribution in the crystal cross section The semiconductor silicon single crystal as described above can be manufactured without changing the quality. Therefore, desired quality can be obtained without impairing the productivity of the semiconductor silicon single crystal.

以下、本発明の実施例及び比較例を示して本発明をより具体的に説明するが、本発明はこれらに限定されるものではない。 Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples of the present invention, but the present invention is not limited thereto.

(実施例)
本発明の半導体シリコン単結晶の製造方法により、FZ法で製造する半導体シリコン単結晶の軸方向の全体で、酸素濃度が4.0×1016atoms/cm〜5.3×1016atoms/cmの範囲に収まるように、結晶直径200mmのFZシリコン単結晶を製造した。
(Example)
According to the method for producing a semiconductor silicon single crystal of the present invention, the oxygen concentration is 4.0×10 16 atoms/cm 3 to 5.3×10 16 atoms/in the entire axial direction of the semiconductor silicon single crystal produced by the FZ method. An FZ silicon single crystal having a crystal diameter of 200 mm was manufactured so as to be within the range of cm 3 .

まず、原料としてCZシリコン結晶を準備し、このCZシリコン結晶の軸方向の酸素濃度を予め測定して酸素濃度分布を取得した。このときの、予め測定した長手方向の酸素濃度変化は図4の通りであった。 First, a CZ silicon crystal was prepared as a raw material, and the oxygen concentration in the axial direction of this CZ silicon crystal was measured in advance to obtain an oxygen concentration distribution. The change in oxygen concentration in the longitudinal direction measured in advance at this time is as shown in FIG.

次に、図4に示す原料の酸素濃度変化から、結晶成長方向の酸素濃度変化を抑えるために必要な原料供給速度変化に応じた原料直径の変化を計算した。図6は直胴開始時の原料直径を1.0として原料長手方向の直径変化割合を示したものである。このように、酸素濃度が高い位置の直径に比べて、酸素濃度が低い位置の直径が小さくなるように原料のCZシリコン結晶を加工した。 Next, from the change in the oxygen concentration of the raw material shown in FIG. 4, the change in the raw material diameter according to the change in the raw material supply rate necessary to suppress the change in the oxygen concentration in the crystal growth direction was calculated. FIG. 6 shows the rate of change in diameter in the longitudinal direction of the raw material, with the raw material diameter at the start of the straight body being 1.0. In this way, the raw material CZ silicon crystal was processed so that the diameter at the position where the oxygen concentration was low was smaller than the diameter at the position where the oxygen concentration was high.

そして、この形状を加工したCZシリコン結晶を原料として用い、FZ法により半導体シリコン単結晶の製造を行った。このとき、上軸の下降速度を徐々に上げること以外は、直胴中の製造条件を一定として製造した。この時の、メルト滞留時間、メルト表面積、炉内圧力から算出したKの値は18.6であった。(この場合、FZシリコン単結晶/原料棒の酸素導入率は2.7%と計算された) Then, a semiconductor silicon single crystal was manufactured by the FZ method using the CZ silicon crystal processed into this shape as a raw material. At this time, the manufacturing conditions in the straight body were constant except that the descending speed of the upper shaft was gradually increased. At this time, the value of K calculated from the melt residence time, the melt surface area, and the furnace pressure was 18.6. (In this case, the oxygen introduction rate of the FZ silicon single crystal/raw material rod was calculated to be 2.7%)

取得した結晶を任意の間隔でサンプリングし各位置で酸素濃度を測定した結果、図7に示すような酸素濃度範囲となった。図7に示すように、FZ法により製造した半導体シリコン単結晶全体での酸素濃度の最大値は5.3×1016atoms/cm、最小値は4.1×1016atoms/cmとなり、全体が所望とする酸素濃度範囲に収まるような結晶が取得できた。 The obtained crystals were sampled at arbitrary intervals and the oxygen concentration was measured at each position. As a result, the oxygen concentration range was as shown in FIG. 7. As shown in FIG. 7, the maximum value of the oxygen concentration in the entire semiconductor silicon single crystal produced by the FZ method is 5.3×10 16 atoms/cm 3 , and the minimum value is 4.1×10 16 atoms/cm 3 . , A crystal was obtained in which the whole fell within the desired oxygen concentration range.

(比較例)
実施例で使用した原料と長手方向の酸素濃度変化がほぼ同等のCZシリコン結晶を原料として用い、実施例のような形状の加工を行わなかったこと、従って、上軸速度は従来通りとすること以外は、実施例と同条件で、結晶直径200mmのFZシリコン単結晶の製造を行った。
(Comparative example)
The CZ silicon crystal whose oxygen concentration change in the longitudinal direction was almost the same as that of the raw material used in the example was used as the raw material, and the shape as in the example was not processed. Therefore, the upper shaft speed should be the same as before. An FZ silicon single crystal having a crystal diameter of 200 mm was manufactured under the same conditions as in Example except for the above.

比較例の結晶製造により取得した結晶から任意の間隔でサンプリングし各位置で酸素濃度を測定した結果、図8に示すような酸素濃度範囲となった。結晶全体での酸素濃度の最大値は5.2×1016atoms/cm、最小値は3.6×1016atoms/cmであった。 As a result of sampling the crystals obtained by the crystal production of the comparative example at arbitrary intervals and measuring the oxygen concentration at each position, the oxygen concentration range was as shown in FIG. The maximum value of oxygen concentration in the entire crystal was 5.2×10 16 atoms/cm 3 , and the minimum value was 3.6×10 16 atoms/cm 3 .

なお、本発明は、上記実施形態に限定されるものではない。上記実施形態は例示であり、本発明の特許請求の範囲に記載された技術的思想と実質的に同一な構成を有し、同様な作用効果を奏するものは、いかなるものであっても本発明の技術的範囲に包含される。 The present invention is not limited to the above embodiment. The above-described embodiment is an exemplification, and the invention having substantially the same configuration as the technical idea described in the scope of the claims of the present invention and exhibiting the same action and effect is the present invention It is included in the technical scope of.

10…半導体シリコン単結晶製造装置、 11…チャンバー、 12…上軸、
13…下軸、 14…CZシリコン結晶、 15…種結晶、
16…高周波加熱コイル、 17…絞り、 18…溶融帯域、
19…半導体シリコン単結晶、 20…ドープノズル、 21…直胴部、
22…コーン部。
DESCRIPTION OF SYMBOLS 10... Semiconductor silicon single crystal manufacturing apparatus, 11... Chamber, 12... Upper axis,
13... Lower axis, 14... CZ silicon crystal, 15... Seed crystal,
16... High-frequency heating coil, 17... Drawing, 18... Melting zone,
19... Semiconductor silicon single crystal, 20... Dope nozzle, 21... Straight body part,
22... Cone part.

Claims (7)

CZ法により製造したCZシリコン結晶を原料としたFZ法による半導体シリコン単結晶の製造方法において、
前記CZシリコン結晶の軸方向の酸素濃度を予め測定して酸素濃度分布を取得する工程と、
前記取得したCZシリコン結晶の軸方向の酸素濃度分布に応じて、前記CZシリコン結晶の形状を加工する工程と、
前記形状を加工したCZシリコン結晶を原料として用い、FZ法により前記半導体シリコン単結晶を製造する工程とを有することを特徴とするFZ法による半導体シリコン単結晶の製造方法。
In a method for producing a semiconductor silicon single crystal by the FZ method using a CZ silicon crystal produced by the CZ method as a raw material,
Preliminarily measuring the oxygen concentration in the axial direction of the CZ silicon crystal to obtain an oxygen concentration distribution,
Processing the shape of the CZ silicon crystal according to the obtained oxygen concentration distribution in the axial direction of the CZ silicon crystal;
And a step of producing the semiconductor silicon single crystal by the FZ method, using the CZ silicon crystal of which the shape is processed as a raw material, the method of producing the semiconductor silicon single crystal by the FZ method.
前記CZシリコン結晶の形状を加工する工程において、
前記取得したCZシリコン結晶の軸方向の酸素濃度分布に相関するように、前記CZシリコン結晶の直径を軸方向で変化させるように加工することを特徴とする請求項1に記載の半導体シリコン単結晶の製造方法。
In the step of processing the shape of the CZ silicon crystal,
2. The semiconductor silicon single crystal according to claim 1, wherein the CZ silicon crystal is processed so that the diameter of the CZ silicon crystal is changed in the axial direction so as to be correlated with the obtained oxygen concentration distribution of the CZ silicon crystal. Manufacturing method.
前記CZシリコン結晶の形状を加工する工程において、
前記取得したCZシリコン結晶の軸方向の酸素濃度分布における、前記酸素濃度が高い位置の前記CZシリコン結晶の直径に比べて、前記酸素濃度が低い位置の前記CZシリコン結晶の直径が小さくなるように加工することを特徴とする請求項2に記載の半導体シリコン単結晶の製造方法。
In the step of processing the shape of the CZ silicon crystal,
In the axial oxygen concentration distribution of the obtained CZ silicon crystal, the diameter of the CZ silicon crystal at the low oxygen concentration position is smaller than the diameter of the CZ silicon crystal at the high oxygen concentration position. The method for producing a semiconductor silicon single crystal according to claim 2, wherein the method is performed.
前記FZ法で製造する半導体シリコン単結晶の直径を150mm以上とすることを特徴とする請求項1から請求項3のいずれか一項に記載の半導体シリコン単結晶の製造方法。 The method for producing a semiconductor silicon single crystal according to claim 1, wherein a diameter of the semiconductor silicon single crystal produced by the FZ method is 150 mm or more. 所望とする前記FZ法で製造する半導体シリコン単結晶の酸素濃度の50倍以上の酸素濃度を有する前記CZシリコン結晶を原料として用いることを特徴とする請求項1から請求項4のいずれか一項に記載の半導体シリコン単結晶の製造方法。 5. The CZ silicon crystal having an oxygen concentration of 50 times or more the desired oxygen concentration of the semiconductor silicon single crystal produced by the FZ method is used as a raw material. A method for producing a semiconductor silicon single crystal according to 1. 前記FZ法で製造する半導体シリコン単結晶の軸方向の全体で、酸素濃度が2.1×1016atoms/cm以上8.0×1016atoms/cm以下の範囲であることを特徴とする請求項1から請求項5のいずれか一項に記載の半導体シリコン単結晶の製造方法。 The semiconductor silicon single crystal produced by the FZ method has an oxygen concentration of 2.1×10 16 atoms/cm 3 or more and 8.0×10 16 atoms/cm 3 or less in the entire axial direction. The method for producing a semiconductor silicon single crystal according to any one of claims 1 to 5. 前記FZ法で製造する半導体シリコン単結晶の軸方向の全体で、酸素濃度が4.0×1016atoms/cm以上5.0×1016atoms/cm以下の範囲であることを特徴とする請求項6に記載の半導体シリコン単結晶の製造方法。 The semiconductor silicon single crystal produced by the FZ method as a whole has an oxygen concentration in the range of 4.0×10 16 atoms/cm 3 or more and 5.0×10 16 atoms/cm 3 or less in the entire axial direction. The method for producing a semiconductor silicon single crystal according to claim 6.
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