JP2010245376A - Cleaning device for contaminated component in nitride semiconductor manufacturing apparatus - Google Patents

Cleaning device for contaminated component in nitride semiconductor manufacturing apparatus Download PDF

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JP2010245376A
JP2010245376A JP2009093908A JP2009093908A JP2010245376A JP 2010245376 A JP2010245376 A JP 2010245376A JP 2009093908 A JP2009093908 A JP 2009093908A JP 2009093908 A JP2009093908 A JP 2009093908A JP 2010245376 A JP2010245376 A JP 2010245376A
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cleaning
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reaction chamber
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gas
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JP5277054B2 (en
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Shuichi Koseki
修一 小関
Yuichiro Kitamura
祐一郎 北村
Takeshi Ochi
猛 落
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Taiyo Nippon Sanso Corp
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<P>PROBLEM TO BE SOLVED: To provide a reaction furnace for a dry cleaning device which is superior in economy by reducing a supply amount of cleaning gas by improving the efficiency of a cleaning processing for an object to be cleaned. <P>SOLUTION: The device for cleaning the contaminated component of a nitride semiconductor manufacturing apparatus includes a reaction chamber 8 having a cleaning gas introduction pipe 16 and a gas exhaust pipe 20, a support means 4 of supporting the contaminated component 22 in the reaction chamber 8, heat shielding members 7a, 7b configured to hold the contaminated component 22 at high temperature in the reaction chamber 8, and a heating means 3 of heating the inside of the reaction chamber 8, the cleaning gas introduction pipe 16 being arranged at a lower position in the reaction chamber 8. Consequently, the cleaning gas supplied from a lower part in the reaction chamber 8 is heated by the heating means 3 to move up and then efficiently react on contaminants on the contaminated component 22, thereby efficiently cleaning the contaminated component 22. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、半導体製造装置における汚染部品の洗浄装置に関するものであり、さらに詳しくは、窒化物半導体の製造時にウェハー以外の部材に付着した窒化物を洗浄する窒化物半導体製造装置における汚染部品の洗浄装置に関する。   The present invention relates to a cleaning apparatus for contaminated parts in a semiconductor manufacturing apparatus, and more specifically, cleaning of contaminated parts in a nitride semiconductor manufacturing apparatus that cleans nitride adhering to a member other than a wafer during the manufacture of a nitride semiconductor. Relates to the device.

青色発光ダイオード等の電子部品等に利用されている窒化物半導体は、半導体製造装置内においてサファイヤ基板等のウェハー表面に窒化ガリウム(GaN)や窒化ガリウムアルミニウム(AlGaN)等の窒化物を積層させて構成されている。窒化物半導体を製造する際は、均一な厚みの窒化物の薄膜をウェハーに積層させる必要があるため、従来から、ウェハーの表面に均一に窒化物を積層させるように、原料ガスを吹き付けるための工夫が行われている。
原料ガスとしては、トリメチルガリウム(TMG)、トリメチルアルミニウム(TMA)等の有機金属ガスとアンモニア、ホスフィン、アルシン等の水素化合物等が挙げられる。
Nitride semiconductors used for electronic components such as blue light emitting diodes are made by laminating nitrides such as gallium nitride (GaN) and gallium aluminum nitride (AlGaN) on the surface of a wafer such as a sapphire substrate in a semiconductor manufacturing apparatus. It is configured. When manufacturing a nitride semiconductor, it is necessary to laminate a nitride thin film with a uniform thickness on a wafer. Conventionally, a material gas is sprayed so as to laminate nitride uniformly on the surface of a wafer. Ingenuity has been made.
Examples of the source gas include organometallic gases such as trimethylgallium (TMG) and trimethylaluminum (TMA) and hydrogen compounds such as ammonia, phosphine, and arsine.

しかし、原料ガスは、ウェハーの表面だけではなく、半導体製造装置内においてウェハーを保持するウェハートレー等のようなウェハー以外の部品にも吹き付けられる。また、原料ガスを供給するフローチャネル等の部品は、原料ガスと触れる頻度が極めて高い。このため、これらウェハー以外の部品の表面には汚染物が積層しやすく、定期的に洗浄しなければならないという問題があった。
通常は、これらウェハー以外の部品の洗浄は、水素洗浄や燐酸洗浄によって行われる。水素洗浄は、半導体製造装置内において、例えばウェハートレーを1000℃以上の高温に保持しながら水素を通気して洗浄する方法であり、また燐酸洗浄は、半導体製造装置とは別の洗浄装置において、半導体製造装置から取り外されたフローチャネル等の流路形成部品や複雑な形状の部品を加熱した燐酸に浸漬して洗浄する方法である。
However, the source gas is sprayed not only on the surface of the wafer but also on components other than the wafer, such as a wafer tray for holding the wafer in the semiconductor manufacturing apparatus. In addition, parts such as a flow channel for supplying a raw material gas are extremely frequently in contact with the raw material gas. For this reason, there is a problem that contaminants are easily stacked on the surfaces of parts other than these wafers and must be cleaned periodically.
Usually, these parts other than the wafer are cleaned by hydrogen cleaning or phosphoric acid cleaning. In the semiconductor manufacturing apparatus, hydrogen cleaning is a method in which, for example, a wafer tray is maintained at a high temperature of 1000 ° C. or higher while hydrogen is passed through, and phosphoric acid cleaning is performed in a cleaning apparatus separate from the semiconductor manufacturing apparatus. In this method, a flow path forming component such as a flow channel removed from a semiconductor manufacturing apparatus or a component having a complicated shape is immersed in heated phosphoric acid for cleaning.

しかし、水素洗浄の場合には、ウェハートレーを1000℃以上の高温に保持しなければならないため、ウェハートレーが熱変形する恐れがあるという問題があった。また、燐酸洗浄の場合には、有毒な燐酸を加熱して用いることから、燐酸の蒸気により洗浄作業者が危険に曝されるという問題があった。   However, in the case of hydrogen cleaning, since the wafer tray must be kept at a high temperature of 1000 ° C. or higher, there is a problem that the wafer tray may be thermally deformed. Further, in the case of cleaning with phosphoric acid, since toxic phosphoric acid is heated and used, there is a problem that the cleaning worker is exposed to danger by the vapor of phosphoric acid.

このような問題点を解決するために、ウェハートレー等の部品を損傷させず、かつ作業者が安全に作業できる洗浄装置や方法が提案されている(例えば、特許文献1参照)。特許文献1に示す洗浄装置は、具体的には図3に示すような構造を備えたものとして実施されている。以下、従来の洗浄装置について図3に基づき説明する。   In order to solve such problems, there has been proposed a cleaning apparatus and method that allow an operator to work safely without damaging components such as a wafer tray (see, for example, Patent Document 1). Specifically, the cleaning apparatus shown in Patent Document 1 is implemented as having a structure as shown in FIG. Hereinafter, a conventional cleaning apparatus will be described with reference to FIG.

洗浄装置101は、反応管102及び加熱装置103を備えている。反応管102は、両端に第1蓋部104と第2蓋部105を取付固定した円筒形状の筒型部材であり、内部には、反応室106が形成されている。反応室106内には、支持部材107と、2枚の遮熱板108とが設けられている。   The cleaning device 101 includes a reaction tube 102 and a heating device 103. The reaction tube 102 is a cylindrical member having a first lid 104 and a second lid 105 attached and fixed at both ends, and a reaction chamber 106 is formed inside. In the reaction chamber 106, a support member 107 and two heat shield plates 108 are provided.

第1蓋部104は、正面から見た場合における中心部に、洗浄ガスを反応室106内へ供給する洗浄ガス導入管109を有している。洗浄ガスには、例えば塩素系ガスが用いられる。第2蓋部105は、正面から見た場合における中心部に、反応室106内において洗浄ガスと汚染部品における汚染物との反応により生成された反応生成物ガスを排出するガス排出管110を有している。
支持部材107は、汚染部品111を支持するとともに、反応室106内の所定位置に汚染部品111を配置するための部材であり、遮熱板108は、支持部材107の左右両側方に設けられ、反応室106内の温度を短時間で上昇できるようになっている。
The first lid 104 has a cleaning gas introduction pipe 109 that supplies a cleaning gas into the reaction chamber 106 at the center when viewed from the front. For example, a chlorine-based gas is used as the cleaning gas. The second lid portion 105 has a gas exhaust pipe 110 that exhausts the reaction product gas generated by the reaction between the cleaning gas and the contaminants in the contaminated parts in the reaction chamber 106 at the center when viewed from the front. is doing.
The support member 107 is a member for supporting the contaminated component 111 and arranging the contaminated component 111 at a predetermined position in the reaction chamber 106. The heat shield plates 108 are provided on both the left and right sides of the support member 107. The temperature in the reaction chamber 106 can be increased in a short time.

このような構成の従来の洗浄装置101においては、汚染物が付着した汚染部品111を適宜方法によって支持部材107に載置した後、加熱装置103によって反応室106内を500〜1000℃の適宜温度まで加熱する。その後、洗浄ガスの供給の開始により洗浄ガス導入管109から反応室106内に導入された洗浄ガスは、汚染部品111に付着した汚染物と反応して反応生成物を生じる。この反応生成物は、反応室106内の温度が500〜1000℃の適宜温度まで上昇しているため、生成後直ちに気化して反応生成物ガスとなり、ガス排出管110から排出される。   In the conventional cleaning apparatus 101 having such a configuration, the contaminated component 111 to which the contaminant is attached is placed on the support member 107 by an appropriate method, and then the reaction apparatus 106 is heated to an appropriate temperature of 500 to 1000 ° C. by the heating apparatus 103. Until heated. Thereafter, the cleaning gas introduced from the cleaning gas introduction pipe 109 into the reaction chamber 106 by the start of the supply of the cleaning gas reacts with contaminants attached to the contaminated component 111 to generate a reaction product. Since the temperature in the reaction chamber 106 has risen to an appropriate temperature of 500 to 1000 ° C., the reaction product is vaporized immediately after generation to become a reaction product gas and is discharged from the gas discharge pipe 110.

特開2006−332201JP 2006-332201

しかしながら、特許文献1の洗浄装置は、汚染部品の洗浄処理に要する時間が長くなるという問題があった。
これは、特許文献1の洗浄装置は、例えば図3中において、洗浄ガス導入管109から反応室106内へ導入された洗浄ガスが、第1蓋部104の近傍に配置されている遮熱板108に衝突してA方向やB方向に分流し、この分流した洗浄ガスのうち汚染部品111の洗浄に利用できるのは、B方向に流れた洗浄ガスのさらにB1方向に流れたもののみであって、非常に洗浄の効率が悪いことが原因となっている。
However, the cleaning device of Patent Document 1 has a problem that the time required for cleaning the contaminated parts becomes long.
This is because, for example, in the cleaning apparatus of Patent Document 1, the cleaning gas introduced into the reaction chamber 106 from the cleaning gas introduction pipe 109 is disposed in the vicinity of the first lid 104 in FIG. The cleaning gas that collides with 108 and diverts in the A direction and the B direction. Of the diverted cleaning gas, only the cleaning gas that has flowed in the B direction further flows in the B1 direction. This is because the cleaning efficiency is very poor.

A方向に流れた洗浄ガスのほとんどが汚染部品111の洗浄に利用できないのは、従来の洗浄装置101は、加熱された洗浄ガスが熱対流によって反応室106の下部から上部へと移動することを利用しており、反応室106内において既に汚染部品111の上方を流れている洗浄ガスは下方へ流れないからである。また、B方向に流れた洗浄ガスは、反応室106内で加熱された全てがB1方向に流れるわけではなく、B2方向に流れるものもあるため、洗浄処理の効率が悪化し、洗浄時間が長くなる原因となっている。   The fact that most of the cleaning gas flowing in the direction A cannot be used for cleaning the contaminated part 111 is that the conventional cleaning apparatus 101 is that the heated cleaning gas moves from the lower part to the upper part of the reaction chamber 106 by heat convection. This is because the cleaning gas that has been used and has already flowed above the contaminated component 111 in the reaction chamber 106 does not flow downward. Also, the cleaning gas that has flowed in the B direction does not flow in the B1 direction, and all of the gas heated in the reaction chamber 106 flows in the B2 direction, so that the efficiency of the cleaning process is deteriorated and the cleaning time is long. It has become a cause.

洗浄時間が長くなる問題は、洗浄ガスの供給量を増やすことによって解決することはできるものの、この場合には汚染物の洗浄に利用されなかった洗浄ガスが大量に排出されることになる。この場合は、洗浄ガスとして使用する塩素系ガスが強い毒性を持っているため、反応室106から排出されたガスの無害化処理を行う設備の大型化が必要となる。このため、設備の設置や維持に必要なコストが非常に大きくなってしまい、不経済であるという問題が生じる。また、洗浄ガスの供給量が増えることによって洗浄処理のコストが上昇するという問題も生じる。   Although the problem that the cleaning time becomes long can be solved by increasing the supply amount of the cleaning gas, in this case, a large amount of cleaning gas that has not been used for cleaning the contaminants is discharged. In this case, since the chlorine-based gas used as the cleaning gas has strong toxicity, it is necessary to increase the size of the facility for performing the detoxification process of the gas discharged from the reaction chamber 106. For this reason, the cost required for installation and maintenance of facilities becomes very large, which causes a problem of being uneconomical. Further, there is a problem that the cost of the cleaning process increases due to an increase in the supply amount of the cleaning gas.

本発明は、このような問題点に鑑みてなされたものであり、汚染部品の洗浄処理を効率的に行うことで洗浄時間を短縮化でき、かつ洗浄ガスの供給量も減らすことが可能で、経済性にも優れた窒化物半導体製造装置における汚染部品の洗浄装置を提供することを目的とする。   The present invention has been made in view of such problems, and it is possible to shorten the cleaning time by efficiently performing the cleaning process of the contaminated parts, and it is also possible to reduce the supply amount of the cleaning gas, An object of the present invention is to provide a cleaning apparatus for contaminated parts in a nitride semiconductor manufacturing apparatus excellent in economic efficiency.

本発明は、
(1)窒化物半導体製造装置における汚染部品を洗浄する装置であって、洗浄ガス導入管とガス排出管を有する反応室と、前記反応室内で汚染部品を支持する支持手段と、汚染部品を反応室内で高温に保持するための遮熱部材と、反応室内を加熱する加熱手段とを備え、前記洗浄ガス導入管を反応室内の下部に配置したことを特徴とする窒化物半導体製造装置における汚染部品の洗浄装置、
(2)洗浄ガス導入管の先端部が支持手段の下方に位置するように洗浄ガス導入管を配置した上記(1)記載の窒化物半導体製造装置における汚染部品の洗浄装置、
(3)洗浄ガス導入管の先端部が支持手段の下面に向けて立ち上がるように湾曲形成した上記(2)記載の窒化物半導体製造装置における汚染部品の洗浄装置、
(4)支持手段の左右両側方に遮熱部材を設け、一方の遮熱部材と他方の遮熱部材との間の空間を、汚染部品における汚染物と洗浄ガスとが反応する反応領域として構成した上記(1)〜(3)のいずれかに記載の窒化物半導体製造装置における汚染部品の洗浄装置、
(5)洗浄ガス導入管は、遮熱部材の下部近傍を通って反応領域内に導かれ、該洗浄ガス導入管の先端部が支持手段の下方に位置するように配置される上記(4)記載の窒化物半導体製造装置における汚染部品の洗浄装置、
(6)反応室は、横型の中空円筒形状を有する上記(1)〜(5)のいずれかに記載の窒化物半導体製造装置における汚染部品の洗浄装置、
を要旨とする。
The present invention
(1) An apparatus for cleaning contaminated parts in a nitride semiconductor manufacturing apparatus, a reaction chamber having a cleaning gas introduction pipe and a gas discharge pipe, a support means for supporting the contaminated parts in the reaction chamber, and reacting the contaminated parts A contaminated part in a nitride semiconductor manufacturing apparatus, comprising: a heat shielding member for maintaining a high temperature in the chamber; and a heating means for heating the reaction chamber, wherein the cleaning gas introduction pipe is disposed in a lower portion of the reaction chamber Cleaning equipment,
(2) The apparatus for cleaning contaminated parts in the nitride semiconductor manufacturing apparatus according to (1), wherein the cleaning gas introduction pipe is arranged so that the tip of the cleaning gas introduction pipe is positioned below the support means,
(3) A cleaning apparatus for contaminated parts in the nitride semiconductor manufacturing apparatus according to (2), wherein the cleaning gas introduction pipe is curved so that the tip of the cleaning gas introduction pipe rises toward the lower surface of the support means.
(4) Heat shield members are provided on both the left and right sides of the support means, and the space between one heat shield member and the other heat shield member is configured as a reaction region where contaminants and cleaning gas in contaminated parts react. A contaminated part cleaning apparatus in the nitride semiconductor manufacturing apparatus according to any one of (1) to (3),
(5) The cleaning gas introduction pipe is led into the reaction region through the vicinity of the lower part of the heat shield member, and the cleaning gas introduction pipe is disposed so that the tip of the cleaning gas introduction pipe is located below the support means (4) A cleaning apparatus for contaminated parts in the nitride semiconductor manufacturing apparatus described above,
(6) The reaction chamber has a horizontal hollow cylindrical shape, the cleaning device for contaminated parts in the nitride semiconductor manufacturing apparatus according to any one of (1) to (5),
Is the gist.

本発明によれば、洗浄ガス導入管を反応室内の下部に配置したので、反応室内に供給された洗浄ガスは、遮熱部材に衝突して分流することがなく、必ず反応室内の下部から供給される。導入された洗浄ガスは反応室内で加熱手段により加熱され、汚染部品の下方から上方へ移動するので、より多くの洗浄ガスを汚染部品の洗浄に利用することが可能になり、洗浄時間を飛躍的に短縮することができ、洗浄処理の効率を向上させることが可能になる。   According to the present invention, since the cleaning gas introduction pipe is arranged at the lower part of the reaction chamber, the cleaning gas supplied into the reaction chamber does not collide with the heat shield member and is not shunted, and is always supplied from the lower part of the reaction chamber. Is done. The introduced cleaning gas is heated by the heating means in the reaction chamber and moves from the lower side to the upper side of the contaminated part, so that more cleaning gas can be used for cleaning the contaminated part and the cleaning time is dramatically increased. Thus, the efficiency of the cleaning process can be improved.

また、本発明によれば、洗浄ガス導入管の先端部が支持手段の下方に位置するように洗浄ガス導入管を配置したので、より多くの洗浄ガスを汚染部品の下方から上方へ移動させることができ、洗浄時間をより短縮することができ、洗浄処理の効率をより向上させることが可能になる。   Further, according to the present invention, since the cleaning gas introduction pipe is arranged so that the tip of the cleaning gas introduction pipe is positioned below the support means, more cleaning gas can be moved from below to above the contaminated part. Thus, the cleaning time can be further shortened, and the efficiency of the cleaning process can be further improved.

また、本発明によれば、洗浄ガス導入管の先端部が支持手段の下面に向けて立ち上がるように湾曲形成したので、洗浄ガス導入管から供給された洗浄ガスの流れの方向を支持手段の下面に向けることができ、更には支持手段に支持された汚染部品の方へ向けることができる。したがって、より多くの洗浄ガスを汚染部品の方へ向けて流すことが可能になり、汚染部品の洗浄処理の効率をさらに向上させることが可能になる。   Further, according to the present invention, since the tip of the cleaning gas introduction pipe is curved so as to rise toward the lower surface of the support means, the flow direction of the cleaning gas supplied from the cleaning gas introduction pipe is changed to the lower surface of the support means. Or even towards the contaminated part supported by the support means. Therefore, it becomes possible to flow more cleaning gas toward the contaminated part, and it is possible to further improve the efficiency of the cleaning process for the contaminated part.

また、本発明によれば、支持手段の左右両側方に遮熱部材を設け、一方の遮熱部材と他方の遮熱部材との空間を、汚染部品における汚染物と洗浄ガスとが反応する反応領域として構成したので、反応領域内の熱を反応領域外へ逃がすことがなく、反応領域内の温度を短時間で所定の温度まで上昇させ、かつ維持することが可能になる。これにより、反応領域内における汚染部品の洗浄処理をさらに効率的に行うことが可能になり、短時間で洗浄処理を行うことが可能になる。   Further, according to the present invention, the heat shield members are provided on both the left and right sides of the support means, and the reaction between the contaminated parts and the cleaning gas reacts in the space between the one heat shield member and the other heat shield member. Since it is configured as a region, heat in the reaction region is not released outside the reaction region, and the temperature in the reaction region can be raised to a predetermined temperature and maintained in a short time. This makes it possible to more efficiently clean the contaminated parts in the reaction region, and to perform the cleaning process in a short time.

また、本発明によれば、洗浄ガス導入管が遮熱部材の下部近傍を通って反応領域内に導かれ、該洗浄ガス導入管の先端部が支持手段の下方に位置するように配置したので、より多くの洗浄ガスを汚染部品の下方から上方へ移動させることができ、汚染部品の洗浄処理をより効率的に行うことが可能になる。   Also, according to the present invention, the cleaning gas introduction pipe is led into the reaction region through the vicinity of the lower part of the heat shield member, and the tip of the cleaning gas introduction pipe is disposed below the support means. More cleaning gas can be moved from the lower side to the upper side of the contaminated part, and the cleaning process of the contaminated part can be performed more efficiently.

また、本発明によれば、反応室を横型の中空円筒形状にしたので、真空引きした際の反応室の強度を高くすることができ、反応室内を真空にした際に変形する等の不具合を防止することが可能になる。   Further, according to the present invention, since the reaction chamber has a horizontal hollow cylindrical shape, the strength of the reaction chamber when evacuated can be increased, and there is a problem such as deformation when the reaction chamber is evacuated. It becomes possible to prevent.

このように、本発明によれば、汚染部品の洗浄処理の効率を飛躍的に向上させることが可能になるので、従来よりもはるかに少ない量の洗浄ガスを供給して従来と同等の洗浄力を維持することもできる。したがって、従来と同等の洗浄力で洗浄する場合には、洗浄ガスの供給量をはるかに減少させることができるので、洗浄装置から排出された反応生成物ガスや洗浄ガスを無害化する無害化処理設備を小型化することが可能になり、設備や洗浄処理に必要なコストを大幅に低減させることも可能になる。   As described above, according to the present invention, it becomes possible to dramatically improve the efficiency of the cleaning process for contaminated parts. Can also be maintained. Therefore, when cleaning with the same level of cleaning power as before, the supply amount of cleaning gas can be greatly reduced, so the detoxification treatment that makes the reaction product gas and cleaning gas discharged from the cleaning device harmless. The facility can be downsized, and the cost required for the facility and the cleaning process can be greatly reduced.

本発明に係る洗浄装置の反応管を表した概念図である。It is a conceptual diagram showing the reaction tube of the washing | cleaning apparatus which concerns on this invention. 洗浄装置の内部構成と洗浄ガスの流れを表した模式図である。It is the model showing the internal structure of the washing | cleaning apparatus, and the flow of washing | cleaning gas. 従来の洗浄装置の内部構成と洗浄ガスの流れを表した模式図である。It is the schematic diagram showing the internal structure of the conventional cleaning apparatus, and the flow of cleaning gas.

本発明の実施の形態である窒化物半導体製造装置における汚染部品の洗浄装置について、図1及び図2に基づいて説明する。図1は、本発明の実施の形態である洗浄装置の反応管を表した概念図、図2は、洗浄装置の内部構成と洗浄ガス及び反応生成物ガスの流れを表した模式図である。   A contaminated parts cleaning apparatus in a nitride semiconductor manufacturing apparatus according to an embodiment of the present invention will be described with reference to FIGS. FIG. 1 is a conceptual diagram illustrating a reaction tube of a cleaning apparatus according to an embodiment of the present invention, and FIG. 2 is a schematic diagram illustrating an internal configuration of the cleaning apparatus and a flow of cleaning gas and reaction product gas.

洗浄装置1は、反応管2と、反応管2の周囲に上下から設けられた一対の加熱手段としての加熱装置3を備えている。反応管2は、両端にフランジを設けた横型の中空円筒形状を有する筒型部材であり、例えば石英により形成されている。反応管2の内部には、汚染部品22を支持するための支持手段4が設けられている。この支持手段4は保持部材5と支持架台6とから構成されており、支持手段4の左右両側方には遮熱板7a,7bが設けられている。また、反応管2の内部には反応室8が形成されており、この反応室8には、一方の遮熱板7aと他方の遮熱板7bとの間の空間が反応領域9として構成されている。この反応領域9は、後述する汚染物と洗浄ガスとが反応する領域である。   The cleaning device 1 includes a reaction tube 2 and a heating device 3 as a pair of heating means provided around the reaction tube 2 from above and below. The reaction tube 2 is a cylindrical member having a horizontal hollow cylindrical shape having flanges at both ends, and is made of, for example, quartz. Support means 4 for supporting the contaminated component 22 is provided inside the reaction tube 2. The support means 4 includes a holding member 5 and a support base 6, and heat shield plates 7 a and 7 b are provided on both the left and right sides of the support means 4. A reaction chamber 8 is formed inside the reaction tube 2, and a space between one heat shield plate 7 a and the other heat shield plate 7 b is configured as a reaction region 9 in the reaction chamber 8. ing. This reaction region 9 is a region where contaminants described later and cleaning gas react.

保持部材5は、後述する汚染部品22を保持するための部材であり、例えばカーボンや石英により形成されている。この保持部材5は、適宜方法によって載置された汚染部品22を支持することができ、かつその状態を保持できるように構成されている。汚染部品22を保持する構成は、例えば保持部材5の表面に汚染部品22の一部分を挿入できる溝5aを設けておき、汚染部品22をその溝5aへ差し込むことによって実現することができる。なお、この保持の方法はどのような方法を用いてもよく、上述した例には限定されない。   The holding member 5 is a member for holding a contaminated component 22 described later, and is formed of, for example, carbon or quartz. The holding member 5 is configured to support the contaminated component 22 placed by an appropriate method and to hold the state. The configuration for holding the contaminated component 22 can be realized, for example, by providing a groove 5 a into which a part of the contaminated component 22 can be inserted on the surface of the holding member 5 and inserting the contaminated component 22 into the groove 5 a. This holding method may be any method and is not limited to the example described above.

また、保持部材5には、複数の貫通孔5bが形成されており、下方から供給される洗浄ガスが上方向へ流れやすくなるように構成されている。これにより、保持部材5に保持された汚染部品22に洗浄ガスが接触しやすくなり、汚染部品22の洗浄処理が効率的に行えるようになっている。なお、保持部材5が汚染部品22を保持できる強度を維持できるものであれば、貫通孔5bの形状は特に限定されない。例えば、貫通孔5bの形状は四角形や丸形でもよい。また、保持部材5に貫通孔5bを形成する以外に、保持部材5を格子状に形成してもよい。   Further, the holding member 5 is formed with a plurality of through holes 5b so that the cleaning gas supplied from below can easily flow upward. As a result, the cleaning gas can easily come into contact with the contaminated component 22 held by the holding member 5, and the cleaning process of the contaminated component 22 can be performed efficiently. The shape of the through hole 5b is not particularly limited as long as the holding member 5 can maintain the strength capable of holding the contaminated component 22. For example, the shape of the through hole 5b may be a square or a round shape. In addition to forming the through holes 5b in the holding member 5, the holding member 5 may be formed in a lattice shape.

支持架台6は、反応室8内に保持部材5を載置するための架台であり、保持部材5の両端部を支持できる位置に一対で設けられている。これら支持架台6は、板材の一端部と他端部とを互いに反対方向へ直角に折り曲げ成形して形成されている。図2においては、保持部材5の左端部を支持する一方の支持架台6は、垂直に延びる板材の一端部である上端部が保持部材5の左端部へ向けて右方へ延出し、他端部である下端部が遮熱板7aへ向けて左方へ延出するよう直角に折り曲げ成形されている。この下端部には、遮熱板7aとの嵌合が可能な大きさの図示しない溝が設けられている。また、この一方の支持架台6には、上端部と下端部との間に形成された垂直に延びる部分に、後述する洗浄ガス導入管16を挿入できる大きさの孔6aが形成されている。また、図2においては、保持部材5の右端部を支持する他方の支持架台6は、垂直に延びる板材の上端部が保持部材5の右端部へ向けて左方へ延出し、下端部が遮熱板7bへ向けて右方へ延出するように折り曲げ成形されている。この下端部には、遮熱板7bとの嵌合が可能な大きさの図示しない溝が設けられている。これら支持架台6の上端部は平面状になるように形成されており、その上部に保持部材5が載置できるように形成されている。また、支持架台6の下端部も平面状になるように形成されており、反応管2の内周面と当接するように形成されている。   The support bases 6 are bases for mounting the holding member 5 in the reaction chamber 8, and are provided in pairs at positions where both ends of the holding member 5 can be supported. These support bases 6 are formed by bending one end portion and the other end portion of a plate material at right angles in opposite directions. In FIG. 2, one support frame 6 that supports the left end portion of the holding member 5 has an upper end that is one end portion of a vertically extending plate member extending rightward toward the left end portion of the holding member 5, and the other end. The lower end portion which is a portion is bent at a right angle so as to extend leftward toward the heat shield plate 7a. The lower end portion is provided with a groove (not shown) having a size capable of fitting with the heat shield plate 7a. In addition, a hole 6a having a size capable of inserting a cleaning gas introduction pipe 16 to be described later is formed in a vertically extending portion formed between the upper end portion and the lower end portion. In FIG. 2, the other support frame 6 that supports the right end portion of the holding member 5 has an upper end portion of a vertically extending plate material extending leftward toward the right end portion of the holding member 5, and a lower end portion blocking. It is bent so as to extend rightward toward the hot plate 7b. The lower end portion is provided with a groove (not shown) having a size capable of fitting with the heat shield plate 7b. The upper ends of these support bases 6 are formed so as to have a planar shape, and are formed so that the holding member 5 can be placed thereon. Further, the lower end portion of the support frame 6 is also formed to be planar, and is formed so as to contact the inner peripheral surface of the reaction tube 2.

なお、支持架台6は、反応管2内に設けることができ、かつ保持部材5を載置できるものであれば、その構成については特に限定されない。例えば、カーボン又は石英で形成された一対の脚部材を反応管2内の長手方向に設けて、反応管2内において長手方向に延びるカーボン製の2本のレールを脚部材上に設置固定し、このレール上に遮熱板や汚染部品を支持する支持架台を載置してもよい。また、このときの支持架台の形状も特に限定されず、遮熱板の支持架台と汚染部品の支持架台とをそれぞれ別個にしてもよいし、一体化してもよい。   In addition, if the support frame 6 can be provided in the reaction tube 2 and can hold | maintain the holding member 5, the structure will not be specifically limited. For example, a pair of leg members formed of carbon or quartz are provided in the longitudinal direction in the reaction tube 2 and two rails made of carbon extending in the longitudinal direction in the reaction tube 2 are installed and fixed on the leg members, A support frame for supporting the heat shielding plate and the contaminated parts may be placed on the rail. In addition, the shape of the support frame at this time is not particularly limited, and the support frame of the heat shield plate and the support frame of the contaminated part may be made separate or integrated.

遮熱板7a,7bは、汚染部品を反応室6内で高温に保持するためのものであり、保持部材5の左右両側方に設けられている。一方の遮熱板7aは、保持部材5と第1蓋体10の間であって保持部材5寄りの位置に設けられており、例えば下端部が一方の支持架台6に形成された図示しない溝に嵌合されることによって固定されている。他方の遮熱板7bは、保持部材5と第2蓋体11の間であって保持部材5寄りの位置に設けられており、例えば下端部が他方の支持架台6に形成された図示しない溝に嵌合されることによって固定されている。一方の遮熱板7aの下部には、開口部7cが形成されている。この開口部7cは、後述する洗浄ガス導入管16が遮熱板7aの下部近傍を通って反応室8内における反応領域9内に挿入できる大きさに形成されている。
これら遮熱板7a,7bは、加熱装置3によって反応室8内が加熱される際に、効率よく温度を上昇させることができるような部材で形成されており、例えばカーボン等によって形成されている。
The heat shield plates 7 a and 7 b are for holding the contaminated parts at a high temperature in the reaction chamber 6, and are provided on the left and right sides of the holding member 5. One heat shield plate 7 a is provided between the holding member 5 and the first lid 10 and at a position near the holding member 5, for example, a groove (not shown) whose lower end portion is formed in one support frame 6. It is fixed by being fitted to. The other heat shield plate 7b is provided between the holding member 5 and the second lid 11 and near the holding member 5, for example, a groove (not shown) having a lower end formed in the other support frame 6. It is fixed by being fitted to. An opening 7c is formed in the lower part of one heat shield plate 7a. The opening 7c is formed in such a size that a cleaning gas introduction pipe 16 to be described later can be inserted into the reaction region 9 in the reaction chamber 8 through the vicinity of the lower part of the heat shield plate 7a.
These heat shield plates 7a and 7b are formed of a member that can efficiently raise the temperature when the inside of the reaction chamber 8 is heated by the heating device 3, and is formed of, for example, carbon. .

また、遮熱板7a,7bの上端面と反応管2の上部内周面との間には空隙部12,13が設けられている。空隙部12は、遮熱板7aと反応管2の上部内周面との間に設けられており、後述する第1蓋体10と遮熱板7aとの間に形成された第1空間部14と連通するように形成されている。空隙部13は、遮熱板7bと反応管2の上部内周面との間に設けられており、後述する第2蓋体11と遮熱板7bとの間に形成された第2空間部15と連通するように形成されている。   Further, gaps 12 and 13 are provided between the upper end surfaces of the heat shield plates 7 a and 7 b and the upper inner peripheral surface of the reaction tube 2. The gap portion 12 is provided between the heat shield plate 7a and the upper inner peripheral surface of the reaction tube 2, and is a first space portion formed between a first lid 10 and a heat shield plate 7a described later. 14 is formed so as to communicate with 14. The gap 13 is provided between the heat shield 7b and the upper inner peripheral surface of the reaction tube 2, and is a second space formed between the second lid 11 and the heat shield 7b described later. 15 is formed so as to communicate with 15.

なお、本明細書における遮熱板の下部近傍には、遮熱板の下部のみならず遮熱板の下方も含まれる。すなわち、遮熱板7aの下部近傍に位置する開口部7cは、洗浄ガス導入管が反応領域内に導かれるように形成されていればよく、例えば、遮熱板7cの下部に洗浄ガス導入管が挿入できる大きさの開口孔や凹部を形成することで実現することができる。また、遮熱板7aの下端面と反応管2の下部内周面との間に間隙を設け、この間隙に洗浄ガス導入管を挿入してもよい。この場合は、洗浄ガス導入管は、遮熱板7aの下方に位置することになる。   Note that the vicinity of the lower portion of the heat shield plate in this specification includes not only the lower portion of the heat shield plate but also the lower portion of the heat shield plate. That is, the opening 7c located near the lower portion of the heat shield plate 7a only needs to be formed so that the cleaning gas introduction pipe is led into the reaction region. For example, the cleaning gas introduction pipe is provided below the heat shield plate 7c. This can be realized by forming an opening hole or a recess having a size that can be inserted. Further, a gap may be provided between the lower end surface of the heat shield plate 7a and the lower inner peripheral surface of the reaction tube 2, and a cleaning gas introduction pipe may be inserted into this gap. In this case, the cleaning gas introduction pipe is located below the heat shield plate 7a.

反応管2には、第1蓋体10が一方側のフランジにボルトで固定されるとともに、第2蓋体11が他方側のフランジにボルトで固定されている。反応管2は、これら第1蓋体10及び第2蓋体11が固定されることにより、密閉構造となるように構成されている。   In the reaction tube 2, the first lid 10 is fixed to the flange on one side with a bolt, and the second lid 11 is fixed to the flange on the other side with a bolt. The reaction tube 2 is configured to have a sealed structure by fixing the first lid body 10 and the second lid body 11.

第1蓋体10は、ステンレスなどの金属で形成されており、第1蓋体10を正面から見た場合における中心部から径方向へずれた位置に洗浄ガス導入管16を有している。洗浄ガス導入管16は、例えば銅などの適宜金属を用いた金属管で形成されており、第1蓋体10から反応室8内に入り込み、さらに遮熱板7aの下部近傍に形成された開口部7cを通って反応領域9内に導かれた状態で挿入固定されている。   The first lid 10 is made of a metal such as stainless steel, and has a cleaning gas introduction pipe 16 at a position shifted in the radial direction from the center when the first lid 10 is viewed from the front. The cleaning gas introduction pipe 16 is formed of a metal pipe using an appropriate metal such as copper, for example. The cleaning gas introduction pipe 16 enters the reaction chamber 8 from the first lid 10 and is further formed in the vicinity of the lower portion of the heat shield plate 7a. It is inserted and fixed in a state of being guided into the reaction region 9 through the portion 7c.

洗浄ガス導入管16の先端部16aは、反応室8内の下部に配置されており、具体的には、保持部材5の下方に位置するように配置されている。また、先端部16aは、保持部材5の下面に向けて立ち上がるように湾曲形成されており、洗浄ガスが汚染部品22に向けて流れやすくなるように形成されている。
なお、洗浄ガス導入管16と汚染部品22までの高さ方向(図2における上下方向)の位置関係は、洗浄ガスが反応室8内に収容された汚染部品22に対して満遍なく行き渡るようにできる程度の間隔を設けていることが好ましい。
また、洗浄ガス導入管16と汚染部品22との水平方向(図2における左右方向)の位置関係は、先端部16aが支持架台6の下方において孔6a側へ位置するように配置され、先端部16aとガス排出管20との間に、洗浄ガスが反応室8内に収容された汚染部品22に対して満遍なく行き渡るようにできる程度の間隔を設けていることが好ましい。
The distal end portion 16 a of the cleaning gas introduction pipe 16 is disposed at the lower part in the reaction chamber 8, and specifically, is disposed so as to be positioned below the holding member 5. Further, the distal end portion 16 a is curved so as to rise toward the lower surface of the holding member 5, and is formed so that the cleaning gas can easily flow toward the contaminated component 22.
The positional relationship in the height direction (vertical direction in FIG. 2) between the cleaning gas introduction pipe 16 and the contaminated part 22 can be distributed evenly with respect to the contaminated part 22 accommodated in the reaction chamber 8. It is preferable to provide a certain interval.
Further, the positional relationship between the cleaning gas introduction pipe 16 and the contaminated component 22 in the horizontal direction (left-right direction in FIG. 2) is arranged such that the tip end portion 16a is located on the hole 6a side below the support frame 6, and the tip end portion It is preferable that an interval is provided between 16 a and the gas discharge pipe 20 so that the cleaning gas can be evenly distributed to the contaminated parts 22 accommodated in the reaction chamber 8.

洗浄ガス導入管16の後端側端部は、洗浄ガス供給装置17と接続されている。洗浄ガス供給装置17は、反応室8内に供給されて汚染部品22における汚染物を洗浄するための洗浄ガスを供給する装置であり、洗浄ガス導入管16を通じて反応管2内へ順次供給できるようになっている。洗浄ガス供給装置17は、洗浄ガスの主成分である塩素系ガスを供給する塩素系ガス供給部18と、塩素系ガスを希釈する希釈ガス供給部19とから構成されており、洗浄ガスは、塩素系ガスと希釈ガスを混合することにより得られる。この洗浄ガスの洗浄能力は、洗浄ガス中における塩素系ガスの濃度によっても適宜調節することができるようになっている。   The rear end of the cleaning gas introduction pipe 16 is connected to the cleaning gas supply device 17. The cleaning gas supply device 17 is a device that supplies a cleaning gas supplied into the reaction chamber 8 to clean the contaminants in the contaminated component 22 and can be sequentially supplied into the reaction tube 2 through the cleaning gas introduction tube 16. It has become. The cleaning gas supply device 17 includes a chlorine-based gas supply unit 18 that supplies a chlorine-based gas that is a main component of the cleaning gas, and a dilution gas supply unit 19 that dilutes the chlorine-based gas. It can be obtained by mixing chlorine gas and dilution gas. The cleaning ability of the cleaning gas can be adjusted as appropriate depending on the concentration of the chlorine-based gas in the cleaning gas.

ここで、洗浄ガスに用いられる塩素系ガスとしては、Cl(塩素)、HC、SiCl、SiHCl、SiHCl、SiHCl、BCl、CHCl、CHCl、CHCl等の分子内に塩素を含む化合物の1種又は2種以上の混合物が用いられるが、価格等を考慮すると塩素が特に好ましい。 Here, as the chlorine-based gas used for the cleaning gas, Cl 2 (chlorine), HC 1 , SiCl 4 , SiHCl 3 , SiH 2 Cl 2 , SiH 3 Cl, BCl 3 , CHCl 3 , CH 2 Cl 2 , CH 3 one or more mixtures of compounds containing chlorine in the molecule such as Cl is used, but consideration of chlorine prices are particularly preferred.

また、希釈ガスとして用いられるガスとしては、窒素、水素、ヘリウム、アルゴン、空気などの塩素系ガスと反応しない任意のガスの1種又は2種以上の混合ガスを用いることができる。   Moreover, as gas used as dilution gas, the 1 type, or 2 or more types of mixed gas of the arbitrary gas which does not react with chlorine gas, such as nitrogen, hydrogen, helium, argon, and air, can be used.

さらに、洗浄ガス中の塩素系ガス濃度は0.1体積%以上とされる。塩素系ガス濃度が0.1体積%未満でも汚染物は洗浄ガス中の塩素系ガスと反応するが、反応速度が遅くなり実用性に乏しくなる。一方、塩素系ガス濃度は高い方が洗浄能力は高まるものの、塩素系ガス濃度を高くしすぎると、部品自体が腐食する恐れがあるので、通常は50体積%以下とするのが好ましい。   Furthermore, the chlorine-based gas concentration in the cleaning gas is set to 0.1% by volume or more. Even if the chlorine-based gas concentration is less than 0.1% by volume, the contaminants react with the chlorine-based gas in the cleaning gas, but the reaction rate becomes slow and the practicality becomes poor. On the other hand, the higher the chlorine-based gas concentration, the higher the cleaning ability. However, if the chlorine-based gas concentration is too high, there is a risk that the parts themselves corrode.

第2蓋体11は、ステンレスなどの金属で形成されており、第2蓋体11を正面から見た場合の中心部にガス排出管20を有している。反応生成物ガスは、洗浄ガスと汚染部品22における汚染物とが接触した際に生成されるガスであり、これには、汚染部品22の洗浄に利用されずに排出される洗浄ガスが含まれる場合もある。ガス排出管20は、一端部が第2蓋体11に挿入固定され、他端部が無害化処理装置21と接続されており、反応室8内から排出される反応生成物ガスを無害化処理装置21へ移送する銅管等の金属製配管である。無害化処理装置21は、反応生成物ガスに含まれた塩素系ガスなど人体に有害な成分を無害化するための装置である。   The second lid 11 is made of a metal such as stainless steel, and has a gas discharge pipe 20 at the center when the second lid 11 is viewed from the front. The reaction product gas is a gas that is generated when the cleaning gas comes into contact with the contaminants in the contaminated part 22, and includes a cleaning gas that is discharged without being used for cleaning the contaminated part 22. In some cases. One end of the gas discharge pipe 20 is inserted and fixed to the second lid 11, and the other end is connected to the detoxification treatment device 21, and the reaction product gas discharged from the reaction chamber 8 is detoxified. It is a metal pipe such as a copper pipe to be transferred to the device 21. The detoxification treatment device 21 is a device for detoxifying components harmful to the human body such as a chlorine-based gas contained in the reaction product gas.

汚染部品22は、ウェハーの表面に窒化物の薄膜を生成する際に窒化物の薄膜等の汚染物が付着した洗浄対象物であり、例えばウェハートレーやフローチャネル等のようなものである。本実施形態の洗浄装置1においては、汚染部品22がどのような形状であっても洗浄することが可能であるが、本明細書においては、汚染部品22の一例として、表面に汚染物が付着した板材を用いて説明する。   The contaminated component 22 is an object to be cleaned in which a contaminant such as a nitride thin film adheres when a nitride thin film is formed on the surface of the wafer, such as a wafer tray or a flow channel. In the cleaning apparatus 1 of the present embodiment, it is possible to clean the contaminated component 22 in any shape. However, in this specification, as an example of the contaminated component 22, contaminants adhere to the surface. This will be described using the plate material.

次に、本実施の形態の洗浄装置1の作用について説明する。洗浄装置1は、通常は、保持部材5が反応室8内の支持架台6上に載置され、第1蓋体10及び第2蓋体11が取り付けられて密閉されている。汚染部品22を洗浄する際には、まず、保持部材5を反応室8内から取り出す。この作業は、第1蓋体10と、第1蓋体10と対向するように配置された遮熱板7a、或いは、第2蓋体11と、第2蓋体11と対向するように配置された遮熱板7bのいずれかを取り外す。そして、支持架台6上に載置された保持部材5を反応室8から取り出す。   Next, the operation of the cleaning device 1 of the present embodiment will be described. In the cleaning apparatus 1, the holding member 5 is normally placed on the support frame 6 in the reaction chamber 8, and the first lid body 10 and the second lid body 11 are attached and sealed. When cleaning the contaminated part 22, first, the holding member 5 is taken out from the reaction chamber 8. This operation is arranged so as to face the first lid 10 and the heat shield plate 7a arranged to face the first lid 10, or the second lid 11 and the second lid 11. Remove any of the heat shield plates 7b. Then, the holding member 5 placed on the support frame 6 is taken out from the reaction chamber 8.

次に、汚染部品22を保持部材5上に保持する。このとき、保持部材5は、洗浄時に汚染部品22の表面に効率良く洗浄ガスが接触するように配置できるものであることが好ましい。このように配置するには、例えば図2に示すように、汚染部品22を若干傾斜させることによっても実現することができるが、これ以外の配置の仕方によって洗浄ガスと接触しやすくしてもよい。
保持部材5上に汚染部品22を載置したら、保持部材5を反応管2の反応室8内に収容し、支持架台6上に載置する。そして、取り外した遮熱板7a,7bを適宜方法により取付固定した後、取り外したフランジをボルト固定して、反応管2を密閉する。
Next, the contaminated component 22 is held on the holding member 5. At this time, it is preferable that the holding member 5 can be disposed so that the cleaning gas efficiently contacts the surface of the contaminated component 22 during cleaning. For example, as shown in FIG. 2, the arrangement can be realized by slightly inclining the contaminated component 22, but it may be easy to come into contact with the cleaning gas depending on other arrangements. .
When the contaminated component 22 is placed on the holding member 5, the holding member 5 is accommodated in the reaction chamber 8 of the reaction tube 2 and placed on the support frame 6. Then, after the removed heat shield plates 7a and 7b are attached and fixed by an appropriate method, the removed flange is bolted and the reaction tube 2 is sealed.

次に、加熱装置3により反応室8内を500〜1000℃の範囲内で任意に設定された温度まで加熱する。このとき、反応室8は一方の遮熱板7aと他方の遮熱板7bとが保持部材5の両側方に対向配置されており、反応領域9から第1空間部14や第2空間部15へ熱が移動するのを防止することができるので、短時間で反応室8内を所定の温度まで加熱することができる。反応室8が所定温度に到達したら、洗浄ガス供給装置17から洗浄ガス導入管16を介して洗浄ガスを反応室8内に供給する。このとき、洗浄ガス導入管16は、汚染部品22の下方に位置し、且つ開口部が上向きになるように、すなわち先端部16aが保持部材5の下面に向けて立ち上がり、汚染部品22の方へ向くように湾曲形成されているので、洗浄ガス導入管16から噴出する洗浄ガスを強制的に汚染部品22が配置されている方向へ供給することができる。   Next, the inside of the reaction chamber 8 is heated to a temperature arbitrarily set within the range of 500 to 1000 ° C. by the heating device 3. At this time, in the reaction chamber 8, one heat shield plate 7 a and the other heat shield plate 7 b are disposed opposite to both sides of the holding member 5, and the first space portion 14 and the second space portion 15 are formed from the reaction region 9. Therefore, the reaction chamber 8 can be heated to a predetermined temperature in a short time. When the reaction chamber 8 reaches a predetermined temperature, the cleaning gas is supplied into the reaction chamber 8 from the cleaning gas supply device 17 through the cleaning gas introduction pipe 16. At this time, the cleaning gas introduction pipe 16 is positioned below the contaminated component 22 and the opening portion faces upward, that is, the tip end portion 16a rises toward the lower surface of the holding member 5 and moves toward the contaminated component 22. Since it is curved so as to face, the cleaning gas ejected from the cleaning gas introduction pipe 16 can be forcibly supplied in the direction in which the contaminated component 22 is disposed.

このとき、反応室8内が所定の温度まで加熱されていることで、反応室8内に供給された洗浄ガス自身も加熱され、反応室8内で熱対流を生じる。したがって、洗浄ガスは、反応室8内へ導入された時に図2中の矢印の方向へ順次流れ、貫通孔5bを通って汚染部品22が配置された方向に向かって流れる。   At this time, since the reaction chamber 8 is heated to a predetermined temperature, the cleaning gas itself supplied into the reaction chamber 8 is also heated, and heat convection is generated in the reaction chamber 8. Accordingly, when the cleaning gas is introduced into the reaction chamber 8, it sequentially flows in the direction of the arrow in FIG. 2, and flows through the through hole 5b in the direction in which the contaminated component 22 is disposed.

なお、反応室8の温度を500℃以上にするのは、汚染部品22における汚染物に洗浄ガスが接触して生成される反応物(本実施形態の場合には塩化物)を気化して排出するためである。また、500〜1000℃の範囲内であるのは、500℃未満の温度の場合には塩化物を気化させる速度が遅くなり実用的でなく、1000℃を超えた温度の場合には、汚染部品22が熱変形する恐れがあるからである。ただし、1000℃を超える温度であっても、汚染部品22が熱変形しない場合には、1000℃を超える温度まで加熱してもよい。   Note that the temperature of the reaction chamber 8 is set to 500 ° C. or higher because the reaction product (chloride in this embodiment) generated by contact of the cleaning gas with the contamination in the contaminated component 22 is vaporized and discharged. It is to do. Moreover, the temperature within the range of 500 to 1000 ° C. is not practical because the rate of vaporizing chloride is slow when the temperature is less than 500 ° C., and when the temperature exceeds 1000 ° C., the contaminated parts This is because 22 may be thermally deformed. However, even if the temperature exceeds 1000 ° C., the contaminated component 22 may be heated to a temperature exceeding 1000 ° C. if it is not thermally deformed.

このように、洗浄ガス導入管16の形状及び加熱装置3により熱対流が生じた洗浄ガスは、図2中の矢印で示すように、保持部材5の貫通孔5bを通過して汚染部品22の表面における汚染物と接触する。この汚染物は、洗浄ガスが接触することによって反応し、塩化物が生成される。この塩化物は、反応室8内が高温になっていることで生成後直ちに気化されるため、汚染部品22は、洗浄ガスとの接触により表面から汚染物が除去されて清浄になる。一方、気化された反応生成物ガスは、熱対流によって汚染部品22の上方に流れ、空隙部13を通過して第2空間部15内へ流れ、さらに第2空間部15を通過してガス排出管20に流れ込み、無害化処理装置21内に取り込まれて無害化処理される。   Thus, the cleaning gas in which the heat convection is generated by the shape of the cleaning gas introduction pipe 16 and the heating device 3 passes through the through-hole 5b of the holding member 5 as shown by the arrows in FIG. Contact with contaminants on the surface. This contaminant reacts when the cleaning gas comes into contact, and chloride is generated. Since this chloride is vaporized immediately after generation due to the high temperature in the reaction chamber 8, the contaminated component 22 is cleaned by removing the contaminant from the surface by contact with the cleaning gas. On the other hand, the vaporized reaction product gas flows above the contaminated part 22 by thermal convection, passes through the gap portion 13 and flows into the second space portion 15, and further passes through the second space portion 15 to discharge gas. It flows into the pipe 20 and is taken into the detoxification processing device 21 to be detoxified.

このような方法により洗浄された汚染部品22は、洗浄後に反応室8内から取り出される。汚染部品22を取り出す際には、まず、反応室8内を真空引きして、その後窒素ガスを封入する。この真空引きと窒素ガスの封入は、必要に応じて数回行われる。これによって、反応室8内に残留する洗浄ガスや反応生成物ガスを除去し、第1蓋体10と、第1蓋体10と対向するように配置された遮熱板7a、或いは、第2蓋体11と、第2蓋体11と対向するように配置された遮熱板7bのいずれかを取り外す。そして、支持架台6上に載置された保持部材5を反応室8から取り出す。その後、保持部材5に載置された汚染部品22を取り外す。   The contaminated part 22 cleaned by such a method is taken out from the reaction chamber 8 after cleaning. When the contaminated part 22 is taken out, first, the reaction chamber 8 is evacuated and then nitrogen gas is sealed. This vacuuming and nitrogen gas sealing are performed several times as necessary. As a result, the cleaning gas and the reaction product gas remaining in the reaction chamber 8 are removed, and the first lid 10 and the heat shielding plate 7a arranged to face the first lid 10 or the second lid 10 are disposed. Any one of the heat shield 7b disposed so as to face the lid 11 and the second lid 11 is removed. Then, the holding member 5 placed on the support frame 6 is taken out from the reaction chamber 8. Thereafter, the contaminated component 22 placed on the holding member 5 is removed.

なお、本明細書における汚染部品22は、半導体製造装置において汚染物を除去する必要があるものであればよく、ウェハートレーやフローチャネルには限定されない。   The contaminated component 22 in the present specification is not limited to a wafer tray or a flow channel as long as it is necessary to remove contaminants in the semiconductor manufacturing apparatus.

(実施例1)
実施例1は、図2に示す洗浄装置1を用いて洗浄処理能力の実験を行った。ここで、反応管2は、内径が360mm、全長が1100mmのものを使用し、洗浄ガス導入管16は内径が6mmのものを使用した。また、汚染部品22は、約1gの汚染物が付着したものを使用した。
また、反応室8の温度は800度まで加熱し、反応管2内部への洗浄ガスの供給は30分間行った。このときの洗浄ガスには、塩素と窒素の混合ガスを用い、ガス流量は、それぞれ塩素が毎分300ミリリットル、窒素が毎分3リットルとなるようにした。洗浄処理後は、反応室8の温度を室温程度まで冷却し、反応管2内に窒素ガスを封入して窒素置換した後に反応管2の内部から汚染部品22を取り出した。そして、取り出した汚染部品22の状態を確認した。
Example 1
In Example 1, an experiment of the cleaning treatment capability was performed using the cleaning apparatus 1 shown in FIG. Here, the reaction tube 2 having an inner diameter of 360 mm and a total length of 1100 mm was used, and the cleaning gas introduction tube 16 having an inner diameter of 6 mm was used. Moreover, the contaminated part 22 used what about 1g of contaminants adhered.
The temperature of the reaction chamber 8 was heated to 800 ° C., and the cleaning gas was supplied into the reaction tube 2 for 30 minutes. At this time, a mixed gas of chlorine and nitrogen was used as the cleaning gas, and the gas flow rates were such that chlorine was 300 milliliters per minute and nitrogen was 3 liters per minute. After the cleaning process, the temperature of the reaction chamber 8 was cooled to about room temperature, nitrogen gas was sealed in the reaction tube 2 and replaced with nitrogen, and then the contaminated part 22 was taken out of the reaction tube 2. And the state of the taken-out contaminated component 22 was confirmed.

汚染部品22に付着した汚染物の除去に関しては、洗浄処理前の汚染部品22の重量と、洗浄処理後の汚染部品22の重量を測定して、洗浄処理前後の測定値の差から、除去された汚染物の量を算出した。そして、洗浄処理前に付着した汚染物の量(本実施例では約1g)で算出した汚染物の量を割るとともに、その値に百分率を掛けることにより、汚染物の除去効率を計算した。   Regarding the removal of contaminants adhering to the contaminated part 22, the weight of the contaminated part 22 before the cleaning process and the weight of the contaminated part 22 after the cleaning process are measured and removed from the difference between the measured values before and after the cleaning process. The amount of contaminated material was calculated. Then, the contaminant removal efficiency was calculated by dividing the amount of contaminants calculated by the amount of contaminants attached before the cleaning treatment (about 1 g in this example) and multiplying that value by a percentage.

実施例1の洗浄装置1で洗浄処理を行った結果、洗浄処理前は拭き取りで除去できなかった汚染物が汚染部品22の表面に付着していたものの、洗浄処理後には拭き取りやすい粉末状の反応生成物が汚染部品22の表面に付着しており、非常に汚染物が除去しやすい状態になっていた。この反応生成物を拭き取り除去した後に求めた汚染物の除去効率は、約99%であった。また、洗浄処理後の汚染部品22の状態は、汚染物が除去されて非常に良好であった。   As a result of the cleaning process performed by the cleaning apparatus 1 of Example 1, the contaminants that could not be removed by wiping before the cleaning process adhered to the surface of the contaminated component 22, but were easily wiped off after the cleaning process. The product adhered to the surface of the contaminated part 22, and it was very easy to remove the contaminant. The removal efficiency of contaminants determined after wiping and removing this reaction product was about 99%. Further, the state of the contaminated part 22 after the cleaning treatment was very good since the contaminants were removed.

(実施例2)
実施例2は、実施例1と同様の方法により洗浄処理能力の実験を行った。なお、実施例2では、洗浄処理時間を60分にして行った。
洗浄処理を行った結果、洗浄処理前は拭き取りによって除去できなかった汚染物が汚染部品22の表面に付着していたものの、洗浄処理後には拭き取りやすい粉末状の反応生成物が汚染部品22の表面に堆積しており、非常に汚染物が除去しやすい状態になっていた。この反応生成物を拭き取り除去した後に求めた汚染物の除去効率は、約99%であった。また、洗浄処理後の汚染部品22の状態は、汚染物が除去されて非常に良好であった。
(Example 2)
In Example 2, an experiment on the cleaning ability was performed in the same manner as in Example 1. In Example 2, the cleaning treatment time was 60 minutes.
As a result of performing the cleaning process, contaminants that could not be removed by wiping before the cleaning process adhered to the surface of the contaminated part 22, but after the cleaning process, a powdery reaction product that is easy to wipe off is a surface of the contaminated part 22 It was in a state where it was very easy to remove contaminants. The removal efficiency of contaminants determined after wiping and removing this reaction product was about 99%. Further, the state of the contaminated part 22 after the cleaning treatment was very good since the contaminants were removed.

(比較例1)
比較例1は、図3の洗浄装置を用いて実施例1と同じ条件で洗浄処理能力の実験を行った。洗浄処理を行った結果、洗浄処理前には拭き取りによって除去できなかった汚染物が汚染部品22の表面に付着していたものの、洗浄処理後には拭き取りやすい粉末状の反応生成物が汚染部品の表面に蓄積しており、汚染物がとりやすい状態になっていた。しかし、この反応生成物を拭き取り除去した後に求めた汚染物の除去効率は約73%で、汚染物の一部は未反応の状態で残留していた。
(Comparative Example 1)
In Comparative Example 1, an experiment of cleaning ability was performed under the same conditions as Example 1 using the cleaning apparatus of FIG. As a result of the cleaning process, contaminants that could not be removed by wiping before the cleaning process adhered to the surface of the contaminated part 22, but after the cleaning process, a powdery reaction product that was easy to wipe off was found on the surface of the contaminated part. It was in a state where it was easy to remove contaminants. However, the contaminant removal efficiency obtained after wiping and removing the reaction product was about 73%, and a part of the contaminant remained unreacted.

(比較例2)
比較例2は、比較例1と同様の方法により洗浄処理能力の実験を行った。なお、比較例2では、洗浄処理時間を60分にして行った。
洗浄処理を行った結果、洗浄処理前には拭き取りによって除去できなかった汚染物が汚染部品の表面に付着していたものの、洗浄処理後には拭き取りやすい粉末状の反応生成物が汚染部品の表面に蓄積しており、汚染物がとりやすい状態になっていた。この反応生成物を拭き取り除去した後に求めた汚染物の除去効率は約98%であった。
(Comparative Example 2)
In Comparative Example 2, an experiment on the cleaning ability was performed in the same manner as in Comparative Example 1. In Comparative Example 2, the cleaning treatment time was 60 minutes.
As a result of the cleaning process, contaminants that could not be removed by wiping before the cleaning process adhered to the surface of the contaminated part, but after the cleaning process, a powdery reaction product that is easy to wipe off is present on the surface of the contaminated part. Accumulated and easily contaminated. The removal efficiency of contaminants determined after wiping and removing this reaction product was about 98%.

以上のように、本実施の形態の洗浄装置では、洗浄処理開始後30分で約99%の汚染物を除去することが可能であり、洗浄処理時間を60分としても汚染物を除去できるのは99%と同一であった。このことから、本実施の形態の洗浄装置では、洗浄処理を30分行うことで汚染部品22における汚染物を拭き取り除去できる状態にすることができ、そのうちの一部は、洗浄処理中に反応室8内で加熱されることにより反応生成物ガスとして気化させることが可能になる。
一方、比較例1及び2では、汚染部品の汚染物を98%除去するためには洗浄処理を60分行う必要がある。また、洗浄処理を60分行った場合であっても、実施例1及び2のように、汚染物の除去効率を99%にまで向上させることができない。したがって、実施例1及び2の洗浄装置1は、洗浄処理時間の短縮化が可能になるだけでなく、洗浄力も向上させることが可能になる。
As described above, in the cleaning apparatus of this embodiment, it is possible to remove about 99% of contaminants 30 minutes after the start of the cleaning process, and contaminants can be removed even if the cleaning process time is 60 minutes. Was identical to 99%. For this reason, in the cleaning apparatus of the present embodiment, the cleaning process can be performed for 30 minutes so that the contaminants in the contaminated component 22 can be wiped and removed, and part of the reaction chamber can be used during the cleaning process. It becomes possible to evaporate as reaction product gas by heating within 8.
On the other hand, in Comparative Examples 1 and 2, it is necessary to perform a cleaning process for 60 minutes in order to remove 98% of contaminants from contaminated parts. Moreover, even if it is a case where a washing process is performed for 60 minutes, like Example 1 and 2, the removal efficiency of a contaminant cannot be improved to 99%. Therefore, the cleaning apparatuses 1 according to the first and second embodiments can not only shorten the cleaning processing time but also improve the cleaning power.

1 洗浄装置
2 反応管
3 加熱装置
4 支持手段
5 保持部材
6 支持架台
7a,7b 遮熱板
8 反応室
9 反応領域
16 洗浄ガス導入管
16a 先端部
17 ガス排出管
22 汚染部品
DESCRIPTION OF SYMBOLS 1 Cleaning apparatus 2 Reaction tube 3 Heating device 4 Support means 5 Holding member 6 Support stand 7a, 7b Heat shield plate 8 Reaction chamber 9 Reaction area 16 Cleaning gas introduction pipe 16a Tip part 17 Gas discharge pipe 22 Contamination parts

Claims (6)

窒化物半導体製造装置における汚染部品を洗浄する装置であって、洗浄ガス導入管とガス排出管を有する反応室と、前記反応室内で汚染部品を支持する支持手段と、汚染部品を反応室内で高温に保持するための遮熱部材と、反応室内を加熱する加熱手段とを備え、前記洗浄ガス導入管を反応室内の下部に配置したことを特徴とする窒化物半導体製造装置における汚染部品の洗浄装置。   An apparatus for cleaning contaminated parts in a nitride semiconductor manufacturing apparatus, comprising: a reaction chamber having a cleaning gas introduction pipe and a gas exhaust pipe; support means for supporting the contaminated parts in the reaction chamber; An apparatus for cleaning contaminated parts in a nitride semiconductor manufacturing apparatus, comprising: a heat shielding member for holding the heating chamber; and heating means for heating the reaction chamber, wherein the cleaning gas introduction pipe is disposed in a lower portion of the reaction chamber . 洗浄ガス導入管の先端部が支持手段の下方に位置するように洗浄ガス導入管を配置した請求項1記載の窒化物半導体製造装置における汚染部品の洗浄装置。   2. The apparatus for cleaning a contaminated part in a nitride semiconductor manufacturing apparatus according to claim 1, wherein the cleaning gas introduction pipe is arranged so that the tip of the cleaning gas introduction pipe is positioned below the support means. 洗浄ガス導入管の先端部が支持手段の下面に向けて立ち上がるように湾曲形成した請求項2記載の窒化物半導体製造装置における汚染部品の洗浄装置。   The apparatus for cleaning a contaminated part in a nitride semiconductor manufacturing apparatus according to claim 2, wherein the cleaning gas introducing pipe is curved so that the front end portion thereof rises toward the lower surface of the support means. 支持手段の左右両側方に遮熱部材を設け、一方の遮熱部材と他方の遮熱部材との間の空間を、汚染部品における汚染物と洗浄ガスとが反応する反応領域として構成した請求項1〜3のいずれかに記載の窒化物半導体製造装置における汚染部品の洗浄装置。   A heat shield member is provided on both the left and right sides of the support means, and a space between one heat shield member and the other heat shield member is configured as a reaction region where contaminants and cleaning gas in a contaminated part react. A cleaning apparatus for contaminated parts in the nitride semiconductor manufacturing apparatus according to any one of 1 to 3. 洗浄ガス導入管は、遮熱部材の下部近傍を通って反応領域内に導かれ、該洗浄ガス導入管の先端部が支持手段の下方に位置するように配置される請求項4記載の窒化物半導体製造装置における汚染部品の洗浄装置。   The nitride according to claim 4, wherein the cleaning gas introduction pipe is led into the reaction region through the vicinity of the lower portion of the heat shield member, and the tip of the cleaning gas introduction pipe is disposed below the support means. Cleaning equipment for contaminated parts in semiconductor manufacturing equipment. 反応室は、横型の中空円筒形状を有する請求項1〜5のいずれかに記載の窒化物半導体製造装置における汚染部品の洗浄装置。   6. The apparatus for cleaning contaminated parts in a nitride semiconductor manufacturing apparatus according to claim 1, wherein the reaction chamber has a horizontal hollow cylindrical shape.
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CN102637587A (en) * 2011-02-15 2012-08-15 富士通株式会社 Cleaning apparatus for semiconductor manufacturing apparatus and method for manufacturing semiconductor device using the same
WO2012157161A1 (en) 2011-05-19 2012-11-22 古河機械金属株式会社 Method of washing semiconductor manufacturing apparatus component, apparatus for washing semiconductor manufacturing apparatus component, and vapor phase growth apparatus
JP2017209596A (en) * 2016-05-23 2017-11-30 大陽日酸株式会社 Cleaning device of components for vapor phase growth apparatus
WO2020100554A1 (en) * 2018-11-16 2020-05-22 大陽日酸株式会社 Apparatus for cleaning component of semiconductor production apparatus, method for cleaning component of semiconductor production apparatus, and system for cleaning component of semiconductor production apparatus

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Cited By (8)

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Publication number Priority date Publication date Assignee Title
CN102637587A (en) * 2011-02-15 2012-08-15 富士通株式会社 Cleaning apparatus for semiconductor manufacturing apparatus and method for manufacturing semiconductor device using the same
WO2012157161A1 (en) 2011-05-19 2012-11-22 古河機械金属株式会社 Method of washing semiconductor manufacturing apparatus component, apparatus for washing semiconductor manufacturing apparatus component, and vapor phase growth apparatus
US10741380B2 (en) 2011-05-19 2020-08-11 Furukawa Co., Ltd. Method for washing semiconductor manufacturing apparatus component, apparatus for washing semiconductor manufacturing apparatus component, and vapor phase growth apparatus
JP2017209596A (en) * 2016-05-23 2017-11-30 大陽日酸株式会社 Cleaning device of components for vapor phase growth apparatus
WO2020100554A1 (en) * 2018-11-16 2020-05-22 大陽日酸株式会社 Apparatus for cleaning component of semiconductor production apparatus, method for cleaning component of semiconductor production apparatus, and system for cleaning component of semiconductor production apparatus
JP2020088016A (en) * 2018-11-16 2020-06-04 大陽日酸株式会社 Semiconductor manufacturing device component cleaning device, semiconductor manufacturing device component cleaning method, and semiconductor manufacturing device component cleaning system
CN113015583A (en) * 2018-11-16 2021-06-22 大阳日酸株式会社 Cleaning device for semiconductor manufacturing apparatus component, cleaning method for semiconductor manufacturing apparatus component, and cleaning system for semiconductor manufacturing apparatus component
CN113015583B (en) * 2018-11-16 2023-08-11 大阳日酸株式会社 Cleaning device, cleaning method and cleaning system for semiconductor manufacturing device parts

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