JP2020064928A - Method for replacing gas in reactor in vapor phase growth apparatus - Google Patents

Method for replacing gas in reactor in vapor phase growth apparatus Download PDF

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JP2020064928A
JP2020064928A JP2018195095A JP2018195095A JP2020064928A JP 2020064928 A JP2020064928 A JP 2020064928A JP 2018195095 A JP2018195095 A JP 2018195095A JP 2018195095 A JP2018195095 A JP 2018195095A JP 2020064928 A JP2020064928 A JP 2020064928A
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JP7223548B2 (en
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優哉 山岡
Yuya Yamaoka
優哉 山岡
内藤 一樹
Kazuki Naito
一樹 内藤
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Taiyo Nippon Sanso Corp
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Abstract

To provide a method for replacing gas in a reactor in a vapor phase growth apparatus that can suppress the generation of particles and replace gas in the reactor.SOLUTION: Before a reactor 11 in a vapor phase growth apparatus is opened by operating an opening/closing lid 11a for loading and unloading a substrate, a purge gas is introduced into the reactor while continuing an exhaust operation from an exhaust unit such as a normal pressure exhaust path 22 or a vacuum exhaust path 23 that exhausts the gas in the reactor to replace the gas in the reactor with the purge gas from the reactive gas.SELECTED DRAWING: Figure 1

Description

本発明は、気相成長装置における反応炉内ガスの置換方法に関し、詳しくは、反応炉への基板の出し入れを行う際に、反応炉内を反応性ガス雰囲気から不活性ガス雰囲気に置換する気相成長装置における反応炉内ガスの置換方法に関する。   The present invention relates to a method for replacing a gas in a reaction furnace in a vapor phase growth apparatus, and more specifically, a gas for replacing a reactive gas atmosphere in a reaction furnace with an inert gas atmosphere when a substrate is put in and out of a reaction furnace. The present invention relates to a method for replacing gas in a reaction furnace in a phase growth apparatus.

気相成長装置は、反応炉内に設置した基板をあらかじめ設定された温度に加熱するとともに、前記反応炉内に原料ガスを供給することにより、前記基板上に半導体結晶を成長させるもので、基本的に、反応炉内への基板の設置、反応炉の閉塞及び反応炉内の減圧、反応炉内への反応性ガスの供給及び基板の加熱、反応性ガスを供給しながらの原料ガスの供給、結晶成長後の原料ガスの供給停止、反応性ガスを供給しながらの反応炉内の降温、不活性ガスを供給して反応炉内のガスを置換、反応炉内の昇圧、反応炉の開放、反応炉からの基板の取り出し及び新たな基板の設置といった手順を繰り返すバッチ式の装置である。また、前記反応炉は、該反応炉を覆う形状を有するグローブボックス内に収容されており、グローブボックス内に大気圧より高い圧力で窒素等の不活性ガスを流通させることにより、反応炉内への大気の侵入を防止している。   The vapor phase growth apparatus is for growing a semiconductor crystal on the substrate by heating a substrate installed in the reaction furnace to a preset temperature and supplying a source gas into the reaction furnace. Specifically, the substrate is installed in the reaction furnace, the reactor is closed and the reactor is depressurized, the reactive gas is supplied into the reaction furnace and the substrate is heated, and the source gas is supplied while supplying the reactive gas. Stop supply of raw material gas after crystal growth, lower temperature in reaction furnace while supplying reactive gas, replace gas in reaction furnace by supplying inert gas, pressurize in reaction furnace, open reactor It is a batch-type apparatus that repeats the procedure of taking out a substrate from the reaction furnace and installing a new substrate. Further, the reaction furnace is housed in a glove box having a shape covering the reaction furnace, and by passing an inert gas such as nitrogen at a pressure higher than atmospheric pressure into the glove box, To prevent the invasion of the atmosphere.

このような気相成長装置では、半導体基板へのパーティクルの混入の防止、1回の半導体結晶成長に必要な時間の短縮が求められており、従来から様々な対策が提案されている。例えば、均圧弁を設けるとともに、複数の弁を適宜開閉し、反応炉内の圧力をグローブボックス内の圧力と同じ圧力にしてから反応炉を開放することにより、パーティクルの発生を抑制することが行われている(例えば、特許文献1参照。)。   In such a vapor phase growth apparatus, it is required to prevent particles from being mixed into the semiconductor substrate and to shorten the time required for one semiconductor crystal growth, and various measures have been conventionally proposed. For example, it is possible to suppress the generation of particles by providing a pressure equalizing valve, opening and closing a plurality of valves as appropriate to make the pressure inside the reactor equal to the pressure inside the glove box, and then opening the reactor. (For example, see Patent Document 1).

特許第5079902号公報Japanese Patent No. 5079902

しかし、特許文献1に記載された気相成長装置では、反応炉を開放する際に、排気弁や均圧弁を開閉する操作を行うため、通常時と異なるガスの流れが生じることから、パーティクルが発生するおそれがあった。また、反応炉周囲の温度に対して反応炉内の温度が高い状態で反応炉を開放すると、温度差によってガスの対流が生じるため、これに起因してパーティクルが発生するおそれもあった。特に、反応炉からの排気部となる排気系の配管からガスが逆流することによって、より多くのパーティクルが発生するおそれがあった。   However, in the vapor phase growth apparatus described in Patent Document 1, when the reaction furnace is opened, the operation of opening and closing the exhaust valve and the pressure equalizing valve is performed, so that a gas flow different from the normal time occurs, so that particles are generated. It was likely to occur. In addition, if the reaction furnace is opened in a state where the temperature inside the reaction furnace is higher than the temperature around the reaction furnace, gas convection occurs due to the temperature difference, which may cause particles to be generated. In particular, there is a possibility that more particles may be generated due to the reverse flow of the gas from the exhaust system pipe serving as the exhaust unit from the reaction furnace.

そこで本発明は、パーティクルの発生を抑えて反応炉内のガス置換を行うことができる気相成長装置における反応炉内ガスの置換方法を提供することを目的としている。   Therefore, an object of the present invention is to provide a method for replacing gas in a reaction furnace in a vapor phase growth apparatus, which can suppress gas generation and perform gas replacement in the reaction furnace.

上記目的を達成するため、本発明の気相成長装置における反応炉内ガスの置換方法は、不活性ガスが流通しているグローブボックス内に配置した反応炉内から成膜後の基板を取り出すために反応炉を開放する際の気相成長装置における反応炉内のガス置換方法において、前記反応炉内に配置した基板への成膜操作を終了した後、前記反応炉を開放する前に、前記反応炉内のガスを排気する排気部からの排気操作を継続しながら、前記反応炉内にパージガスを導入することにより、前記反応炉内のガスをパージガスに置換することを特徴としている。   In order to achieve the above object, the method for replacing the gas in the reaction furnace in the vapor phase growth apparatus of the present invention, in order to take out the substrate after film formation from the reaction furnace placed in the glove box in which the inert gas is flowing In the gas replacement method in the reaction furnace in the vapor phase growth apparatus when opening the reaction furnace, after completing the film forming operation on the substrate placed in the reaction furnace, before opening the reaction furnace, The gas in the reaction furnace is replaced with the purge gas by introducing the purge gas into the reaction furnace while continuing the exhaust operation from the exhaust unit for exhausting the gas in the reaction furnace.

さらに、本発明の気相成長装置における反応炉内のガス置換方法は、前記排気部が、該排気部を流れるガスのコンダクタンスを調整するコンダクタンス調整手段を備え、前記パージガス供給部から反応炉内へのパージガスの供給量に合わせて排気部のコンダクタンスを調整することを特徴としている。   Further, in the gas replacement method in the reaction furnace in the vapor phase growth apparatus of the present invention, the exhaust part is provided with conductance adjusting means for adjusting the conductance of the gas flowing through the exhaust part, and the purge gas supply part into the reaction furnace. The conductance of the exhaust part is adjusted according to the supply amount of the purge gas.

また、前記反応炉内のガスをパージガスに置換して昇圧した後、反応炉を開放するまでの間に、反応炉内の圧力を低下させることなくグローブボックス内の圧力と同等に保持することを特徴としている。   In addition, after replacing the gas in the reaction furnace with the purge gas and increasing the pressure, it is possible to maintain the pressure in the reaction furnace equal to the pressure in the glove box without lowering the pressure in the reaction furnace before opening the reaction furnace. It has a feature.

特に、前記気相成長装置が、基板上に化合物半導体を形成する化合物半導体形成用の気相成長装置であり、さらに、前記気相成長装置が、MOCVD装置であることを特徴としている。   In particular, the vapor phase growth apparatus is a vapor phase growth apparatus for forming a compound semiconductor for forming a compound semiconductor on a substrate, and further, the vapor phase growth apparatus is a MOCVD apparatus.

加えて、前記パージガスの積算供給量が前記反応炉の内容量よりも多く、かつ、前記反応炉内から排出される反応性ガスの濃度が許容濃度以下になるまで前記反応炉内のガスをパージガスに置換するガス置換操作を行うことを特徴としている。   In addition, the gas in the reaction furnace is purged until the cumulative supply amount of the purge gas is larger than the internal volume of the reaction furnace and the concentration of the reactive gas discharged from the reaction furnace becomes equal to or lower than the allowable concentration. It is characterized by performing a gas replacement operation for replacing the gas.

本発明の気相成長装置における反応炉内ガスの置換方法によれば、排気部からの排気を継続して行っているので、排気部を構成する排気配管からのガスの逆流を生じることがなくなり、パーティクルの発生を抑制することができ、反応炉内へのパーティクルの侵入を防止できる。   According to the method for replacing the gas in the reaction furnace in the vapor phase growth apparatus of the present invention, since the exhaust from the exhaust unit is continuously performed, the back flow of gas from the exhaust pipe constituting the exhaust unit is not generated. Moreover, the generation of particles can be suppressed, and the particles can be prevented from entering the reaction furnace.

本発明の気相成長装置における反応炉内ガスの置換方法を実施可能な気相成長装置の一形態例を示す説明図である。It is explanatory drawing which shows one form example of the vapor phase growth apparatus which can implement the substitution method of the gas in a reaction furnace in the vapor phase growth apparatus of this invention. 反応炉における成膜操作中の状態を示す説明図である。It is explanatory drawing which shows the state during film-forming operation in a reaction furnace. 同じく反応炉を開放した状態を示す説明図である。It is explanatory drawing which similarly shows the state which opened the reaction furnace. 本発明の気相成長装置における反応炉内ガスの置換方法におけるガス置換用プログラムの一例を示すフローチャートである。It is a flow chart which shows an example of the program for gas substitution in the substitution method of the gas in the reaction furnace in the vapor phase growth device of the present invention. 1回の成膜操作における反応炉内へのパージガス及び反応性ガスの供給状態と、反応炉内の温度変化及び圧力変化の一例を示す図である。FIG. 3 is a diagram showing an example of supply states of a purge gas and a reactive gas into the reaction furnace and a temperature change and a pressure change in the reaction furnace in one film forming operation.

図1乃至図5は、本発明の気相成長装置における反応炉内ガスの置換方法を説明するための図であって、図1は、本発明を実施可能な気相成長装置の一形態例を示している。本形態例に示す気相成長装置は、基板上に半導体結晶を成長させるための反応炉11と、該反応炉11を覆うグローブボックス12と、反応炉11及びグローブボックス12にそれぞれ接続された複数のガス供給系統及びガス排気系統とを備えている。   1 to 5 are views for explaining a method for replacing a gas in a reaction furnace in a vapor phase growth apparatus of the present invention, and FIG. 1 is an example of one embodiment of a vapor phase growth apparatus in which the present invention can be carried out. Is shown. The vapor phase growth apparatus shown in this embodiment includes a reaction furnace 11 for growing a semiconductor crystal on a substrate, a glove box 12 that covers the reaction furnace 11, and a plurality of reaction furnaces 11 and a plurality of glove boxes 12 connected to the glove box 12, respectively. It has a gas supply system and a gas exhaust system.

ガス供給系統としては、パージガスや反応性ガスを供給弁13及び流量調節器14を介して反応炉11に各種ガスを供給する反応炉用ガス供給経路15と、窒素ガスを窒素供給弁16を介してグローブボックス12内に供給するグローブボックス用ガス供給経路17とが設けられている。通常、前記パージガスとしては、窒素やアルゴンといった不活性ガスが用いられており、反応性ガスとしては、基板上に半導体結晶を成長させる際に使用するガスであって、半導体結晶の種類に応じて、水素、アンモニア、ケイ素化合物、有機金属化合物などが用いられている。   The gas supply system includes a reactor supply gas supply path 15 for supplying various gases to the reaction furnace 11 through a supply valve 13 and a flow rate controller 14 for a purge gas and a reactive gas, and a nitrogen supply valve 16 for supplying nitrogen gas. And a glove box gas supply path 17 for supplying the gas into the glove box 12. Usually, an inert gas such as nitrogen or argon is used as the purge gas, and the reactive gas is a gas used when growing a semiconductor crystal on a substrate, and is a gas depending on the type of the semiconductor crystal. , Hydrogen, ammonia, silicon compounds, organometallic compounds and the like are used.

グローブボックス12のガス排気系統としては、開閉弁18及び自動弁19を介してグローブボックス12内から窒素ガスを排気するグローブボックス用ガス排気経路20が設けられており、前記自動弁19は、グローブボックス12内の圧力を検出するグローブボックス圧力計21で検出した圧力に応じて開度が調節され、グローブボックス12内の圧力を大気圧より僅かに高い圧力に調節して外部からグローブボックス12内への大気の侵入を防止するようにしている。   The gas exhaust system of the glove box 12 is provided with a glove box gas exhaust path 20 for exhausting nitrogen gas from the inside of the glove box 12 via an opening / closing valve 18 and an automatic valve 19, and the automatic valve 19 is a glove box. The opening degree is adjusted according to the pressure detected by the glove box pressure gauge 21 that detects the pressure inside the box 12, and the pressure inside the glove box 12 is adjusted to a pressure slightly higher than the atmospheric pressure so that the inside of the glove box 12 is adjusted from the outside. We are trying to prevent the invasion of the atmosphere into.

一方、反応炉11のガス排気系統としては、反応炉11内からガスを排気するための常圧排気経路22及び真空排気経路23を有しており、常圧排気経路22には、反応炉11内の圧力が常圧に上昇したときに開く常圧排気弁24が設けられている。また、真空排気経路23には、反応炉11内を減圧状態にするための真空ポンプ25が設けられるとともに、反応炉11内を減圧する際に開弁する減圧弁26と、排気系内の圧力を検出する排気圧力計27の検出圧力に応じて真空排気経路22におけるガスコンダクタンスを調整するための排気調整弁28とが設けられている。   On the other hand, the gas exhaust system of the reaction furnace 11 includes a normal pressure exhaust path 22 and a vacuum exhaust path 23 for exhausting gas from the reaction furnace 11, and the normal pressure exhaust path 22 includes the reaction furnace 11 in the normal pressure exhaust path 22. A normal pressure exhaust valve 24 is provided which opens when the internal pressure rises to normal pressure. Further, the vacuum exhaust path 23 is provided with a vacuum pump 25 for reducing the pressure inside the reaction furnace 11, a pressure reducing valve 26 that opens when the pressure inside the reaction furnace 11 is reduced, and a pressure inside the exhaust system. An exhaust adjusting valve 28 for adjusting the gas conductance in the vacuum exhaust path 22 according to the detected pressure of the exhaust pressure gauge 27 for detecting

図2及び図3に示すように、反応炉11には、基板を出し入れするための開閉蓋11aが設けられており、基板の出し入れを行うとき以外には、図2に示すように、開閉蓋11aは閉じられており、基板の出し入れを行う際には、図3に示すように、開閉蓋11aが開いた状態になる。通常、反応炉11内は、ガス排気系統からの排気が行われており、反応炉11内に供給されたパージガスや反応性ガスは、常圧排気経路22又は及び真空排気経路23から排気されている。ガスの排気を止めた状態で開閉蓋11aを開くと、ガス排気系統とグローブボックス12内との圧力差や温度差により、図3に矢印Aで示すように、ガス排気系統内のガスが逆流することがあり、パーティクルの発生原因となる。   As shown in FIGS. 2 and 3, the reaction furnace 11 is provided with an opening / closing lid 11a for loading / unloading the substrate. As shown in FIG. 2, the opening / closing lid 11a is provided except when the substrate is loaded / unloaded. 11a is closed, and when the substrate is taken in and out, the opening / closing lid 11a is opened as shown in FIG. Normally, the inside of the reaction furnace 11 is exhausted from the gas exhaust system, and the purge gas and the reactive gas supplied into the reaction furnace 11 are exhausted from the normal pressure exhaust path 22 and / or the vacuum exhaust path 23. There is. When the opening / closing lid 11a is opened with the gas exhaust stopped, the gas in the gas exhaust system flows backward as indicated by an arrow A in FIG. 3 due to the pressure difference and the temperature difference between the gas exhaust system and the glove box 12. May occur and cause particles to be generated.

そこで、反応炉11の開閉蓋11aを開くときには、基板への半導体結晶成長を行う自動成長プログラムに組み込まれたガス置換操作を行ってから開閉蓋11aを開くようにしている。このガス置換操作は、図4に示すように、まず、ステップ51にて反応炉(リアクタ)11内にパージガスとして不活性ガスのみが流入しているかを確認する。この時点で反応性ガスが反応炉11内に供給されている場合は、成膜操作が完全に終了していないことを示している。   Therefore, when the opening / closing lid 11a of the reactor 11 is opened, the opening / closing lid 11a is opened after performing a gas replacement operation incorporated in an automatic growth program for growing a semiconductor crystal on a substrate. In this gas replacement operation, as shown in FIG. 4, first, in step 51, it is confirmed whether or not only an inert gas is flowing into the reaction furnace 11 as a purge gas. If the reactive gas is being supplied into the reaction furnace 11 at this point, it means that the film forming operation is not completely completed.

ステップ51で反応炉11内に不活性ガスのみが流入していることが確認できたらステップ52に進み、不活性ガスの流入積算値とあらかじめ設定された規定値とを比較し、流入積算値が規定値を超えたらステップ53に進む。前記規定値は、反応炉11の内容量より大きな値に設定されており、あらかじめシミュレーションなどを行って選定した最適値を前記規定値として設定することができる。   If it is confirmed in step 51 that only the inert gas is flowing into the reaction furnace 11, the process proceeds to step 52, where the inflow integrated value of the inert gas is compared with a preset specified value, and the inflow integrated value is When it exceeds the specified value, the process proceeds to step 53. The specified value is set to a value larger than the internal capacity of the reaction furnace 11, and an optimum value selected by performing simulation in advance can be set as the specified value.

ステップ52で不活性ガスの流入積算値が規定値を超えたときには、ステップ53で反応炉11の温度が反応炉蓋開閉可能温度、本形態例では150℃未満になっているかを確認する。そして、反応炉11の温度が反応炉蓋開閉可能温度未満になっていたときには、ステップ54で自動成長プログラムが実行中ではないこと、すなわち、一連の成膜操作が終了していることを確認することで、反応炉11の開閉蓋11aを開くことが可能となる。前記反応炉蓋開閉可能温度は、反応炉周辺部材の耐熱温度に影響され、例えば、60〜600℃の範囲となるが、これに限るものではない。   When the integrated value of the inflow of the inert gas exceeds the specified value in step 52, it is confirmed in step 53 whether the temperature of the reaction furnace 11 is lower than the temperature at which the reaction furnace lid can be opened and closed, which is 150 ° C. in the present embodiment. Then, when the temperature of the reaction furnace 11 is lower than the temperature at which the reaction furnace lid can be opened and closed, it is confirmed in step 54 that the automatic growth program is not being executed, that is, that a series of film forming operations have been completed. As a result, the opening / closing lid 11a of the reaction furnace 11 can be opened. The temperature at which the reaction furnace lid can be opened and closed is influenced by the heat-resistant temperature of the peripheral members of the reaction furnace, and is, for example, in the range of 60 to 600 ° C., but is not limited thereto.

図5は、1回当たりの成膜操作における反応炉11内の温度、圧力、供給ガスの推移を示すもので、まず、基板を設置後に反応炉11を開閉蓋11aで密封し、反応炉11内の圧力を所定の成膜操作圧力(本例では10kPa)に減圧した状態で、反応炉11内に不活性ガス(窒素)及び反応性ガス(水素、アンモニア)を供給した状態で基板の加熱を開始する(昇温過程)。基板が所定の温度、この場合は1000℃に昇温した状態で所定の半導体結晶の薄膜が成長する(成膜過程)。   FIG. 5 shows changes in the temperature, pressure, and supply gas in the reaction furnace 11 per film forming operation. First, after the substrate is installed, the reaction furnace 11 is sealed with the opening / closing lid 11a, and the reaction furnace 11 is closed. The substrate is heated while the internal pressure is reduced to a predetermined film forming operation pressure (10 kPa in this example), and the inert gas (nitrogen) and the reactive gas (hydrogen, ammonia) are supplied into the reaction furnace 11. Is started (heating process). A thin film of a predetermined semiconductor crystal grows in a state where the substrate is heated to a predetermined temperature, in this case 1000 ° C. (deposition process).

所定の薄膜が成長したときに基板の加熱を終了し、各ガスを流したまま反応炉11内の温度を下げていく(降温過程)。反応炉11内の温度がある程度の温度(本例では265℃)まで低下したら、反応性ガスの供給を停止し、不活性ガスのみを反応炉11内に供給し、反応炉11内の反応性ガスをパージして不活性ガス雰囲気にするガス置換を行う(降温+置換過程)。   When the predetermined thin film has grown, the heating of the substrate is terminated, and the temperature inside the reaction furnace 11 is lowered while each gas is being supplied (cooling process). When the temperature in the reaction furnace 11 has dropped to a certain temperature (265 ° C. in this example), the supply of the reactive gas is stopped, and only the inert gas is supplied to the reaction furnace 11, and the reactivity in the reaction furnace 11 is reduced. Gas replacement is performed by purging the gas into an inert gas atmosphere (cooling down + replacement process).

続いて不活性ガスを供給するとともに、反応炉11内の真空排気量を減少させることにより、反応炉11内の圧力を充圧して所定圧力(本例では100kPa(略大気圧))まで上昇させる(充圧過程)。例えば、反応炉11内の圧力が低いときには排気調整弁28を全開状態として反応炉11内のガスを真空ポンプ25によって排気し、不活性ガスの供給によって反応炉11内の圧力が上昇してきたときに、排気調整弁28を徐々に閉方向に作動させてガスの流れを規制することによって真空ポンプ25による排気量を減少させ、反応炉11内の圧力が常圧に上昇したときに排気調整弁28を全閉状態にするとともに、常圧排気弁24を全開状態にして反応炉11からの排気を常圧排気経路22から行う。   Then, by supplying an inert gas and reducing the vacuum exhaust amount in the reaction furnace 11, the pressure in the reaction furnace 11 is filled and raised to a predetermined pressure (100 kPa (approximately atmospheric pressure in this example)). (Charging process). For example, when the pressure inside the reaction furnace 11 is low, the exhaust control valve 28 is fully opened to exhaust the gas inside the reaction furnace 11 by the vacuum pump 25, and when the pressure inside the reaction furnace 11 rises due to the supply of the inert gas. In addition, the exhaust control valve 28 is gradually operated in the closing direction to regulate the gas flow to reduce the exhaust amount by the vacuum pump 25, and when the pressure in the reaction furnace 11 rises to normal pressure, the exhaust control valve 28 28 is fully closed and the atmospheric pressure exhaust valve 24 is fully opened to exhaust the reaction furnace 11 from the atmospheric pressure exhaust path 22.

このようにして供給された不活性ガスを反応炉11を通して常圧排気経路22から排気することにより、反応炉11内の圧力を所定圧力まで昇圧することができる。反応炉11内が所定圧力に充圧されたら、反応炉11及びグローブボックス12に供給するガス流量を適宜調節して反応炉11内の圧力とグローブボックス12内の圧力とを同等とすることにより、ガスの流れを生じることなく開閉蓋11aを開くことができ、薄膜を成長させた基板を取り出して新たな基板を設置する(リアクタ開過程)。再び開閉蓋11aを閉じて反応炉11を密閉した後、反応性ガスの供給を再開するとともに、反応炉11内の減圧を開始し、最初の昇温過程に戻って同様の過程を繰り返す。   By exhausting the inert gas thus supplied from the atmospheric pressure exhaust path 22 through the reaction furnace 11, the pressure in the reaction furnace 11 can be increased to a predetermined pressure. When the inside of the reaction furnace 11 is filled with a predetermined pressure, the gas flow rate supplied to the reaction furnace 11 and the glove box 12 is appropriately adjusted to make the pressure inside the reaction furnace 11 equal to the pressure inside the glove box 12. The opening / closing lid 11a can be opened without generating a gas flow, the substrate on which the thin film is grown is taken out, and a new substrate is installed (reactor opening process). After closing the opening / closing lid 11a again and sealing the reaction furnace 11, the supply of the reactive gas is restarted, the depressurization in the reaction furnace 11 is started, and the same process is repeated by returning to the first temperature rising process.

各過程において反応炉11への不活性ガスの供給操作と、反応炉11からの排気操作とを常時行うことにより、排気部からのガスの逆流を防止でき、パーティクルが発生して反応炉11内に流入することがなくなる。また、反応炉11内の充圧や減圧を行う際に、排気圧力計27の検出圧力に応じて真空排気経路22におけるガスコンダクタンスを調整することにより、反応炉11内からのガスの排出を円滑に行うことができ、ガス流量の変動に伴うパーティクルの発生を回避することができる。   By constantly performing the operation of supplying the inert gas to the reaction furnace 11 and the operation of exhausting the gas from the reaction furnace 11 in each process, it is possible to prevent the backflow of the gas from the exhaust section, and to generate particles to cause the reaction inside the reaction furnace 11. Will not flow into. Further, when charging or depressurizing the inside of the reaction furnace 11, the gas conductance in the vacuum exhaust path 22 is adjusted according to the pressure detected by the exhaust pressure gauge 27, so that the gas is smoothly discharged from the inside of the reaction furnace 11. Therefore, it is possible to avoid the generation of particles due to the fluctuation of the gas flow rate.

さらに、反応炉11内を充圧した後、反応炉内の圧力を低下させる減圧パージを行うことも従来は行われているが、本発明では、反応炉11内を充圧状態を保持するようにしているので、減圧パージに要する時間が不要になり、1回のサイクルの時間を短縮できる。これにより、パーティクルの発生を回避するとともに、時間短縮を図ることができ、従来に比べて高品質な半導体結晶を効率よく製造することができる。   Furthermore, after the inside of the reaction furnace 11 has been filled up, decompression purging for reducing the pressure inside the reaction furnace has been conventionally performed, but in the present invention, the inside of the reaction furnace 11 is kept filled. Therefore, the time required for the reduced pressure purge becomes unnecessary, and the time for one cycle can be shortened. As a result, generation of particles can be avoided, time can be shortened, and a semiconductor crystal of higher quality than in the past can be efficiently manufactured.

特に、基板上に化合物半導体を形成する化合物半導体形成用の気相成長装置、例えば、MOCVD装置では、反応性ガスとして有機金属化合物を使用するので、本発明ではパーティクルの発生を確実に防止できるとともに、1サイクルの成長時間の短縮を図ることができる。さらに、パージガスとなる不活性ガスの積算供給量を、前記反応炉11の内容量よりも多く、かつ、前記反応炉内から排出される反応性ガスの濃度が許容濃度以下になるまで反応炉11内のガスを不活性ガスに置換するガス置換操作を行うことにより、開閉蓋11aを開いたときに、反応炉11からグローブボックス12内に有害な反応性ガスが流出することを確実に防止できる。   In particular, in a vapor phase growth apparatus for forming a compound semiconductor for forming a compound semiconductor on a substrate, for example, a MOCVD apparatus, since an organometallic compound is used as a reactive gas, the present invention can surely prevent generation of particles. The growth time for one cycle can be shortened. Further, the cumulative supply amount of the inert gas serving as the purge gas is larger than the internal volume of the reaction furnace 11, and the reaction gas discharged from the reaction furnace 11 becomes less than the allowable concentration. By performing a gas replacement operation for replacing the gas in the interior with an inert gas, it is possible to reliably prevent harmful reactive gas from flowing out of the reaction furnace 11 into the glove box 12 when the opening / closing lid 11a is opened. .

11…反応炉、11a…開閉蓋、12…グローブボックス、13…供給弁、14…流量調節器、15…反応炉用ガス供給経路、16…窒素供給弁、17…グローブボックス用ガス供給経路、18…開閉弁、19…自動弁、20…グローブボックス用ガス排気経路、21…グローブボックス圧力計、22…常圧排気経路、23…真空排気経路、24…常圧排気弁、25…真空ポンプ、26…減圧弁、27…排気圧力計、28…排気調整弁   11 ... Reactor, 11a ... Open / close lid, 12 ... Glove box, 13 ... Supply valve, 14 ... Flow controller, 15 ... Reactor gas supply path, 16 ... Nitrogen supply valve, 17 ... Glove box gas supply path, 18 ... Open / close valve, 19 ... Automatic valve, 20 ... Glove box gas exhaust path, 21 ... Glove box pressure gauge, 22 ... Normal pressure exhaust path, 23 ... Vacuum exhaust path, 24 ... Normal pressure exhaust valve, 25 ... Vacuum pump , 26 ... Pressure reducing valve, 27 ... Exhaust pressure gauge, 28 ... Exhaust regulating valve

Claims (6)

不活性ガスが流通しているグローブボックス内に配置した反応炉内から成膜後の基板を取り出すために反応炉を開放する際の気相成長装置における反応炉内のガス置換方法において、前記反応炉内に配置した基板への成膜操作を終了した後、前記反応炉を開放する前に、前記反応炉内のガスを排気する排気部からの排気操作を継続しながら、前記反応炉内にパージガスを導入することにより、前記反応炉内のガスをパージガスに置換することを特徴とする気相成長装置における反応炉内のガス置換方法。   In the gas replacement method in the reaction furnace in the vapor phase growth apparatus when opening the reaction furnace to take out the substrate after film formation from the reaction furnace arranged in the glove box in which the inert gas is flowing, the reaction After finishing the film forming operation on the substrate arranged in the furnace, before opening the reaction furnace, while continuing the exhaust operation from the exhaust unit for exhausting the gas in the reaction furnace, A gas replacement method in a reaction furnace in a vapor phase growth apparatus, wherein the gas in the reaction furnace is replaced with a purge gas by introducing a purge gas. 前記排気部は、該排気部を流れるガスのコンダクタンスを調整するコンダクタンス調整手段を備え、パージガス供給部から反応炉内へのパージガスの供給量に合わせて排気部のコンダクタンスを調整することを特徴とする請求項1記載の気相成長装置における反応炉内のガス置換方法。   The exhaust unit includes conductance adjusting means for adjusting the conductance of the gas flowing through the exhaust unit, and adjusts the conductance of the exhaust unit in accordance with the amount of purge gas supplied from the purge gas supply unit into the reaction furnace. The method for gas replacement in the reaction furnace in the vapor phase growth apparatus according to claim 1. 前記反応炉内のガスをパージガスに置換して昇圧した後、反応炉を開放するまでの間に、反応炉内の圧力を低下させることなくグローブボックス内の圧力と同等に保持することを特徴とする請求項1又は2記載の気相成長装置における反応炉内のガス置換方法。   After replacing the gas in the reaction furnace with a purge gas and increasing the pressure, until the reaction furnace is opened, the pressure in the reaction furnace is maintained at the same level as the pressure in the glove box without decreasing. The method for gas replacement in the reaction furnace in the vapor phase growth apparatus according to claim 1 or 2. 前記気相成長装置は、基板上に化合物半導体を形成する化合物半導体形成用の気相成長装置であることを特徴とする請求項1乃至3のいずれか1項記載の気相成長装置における反応炉内のガス置換方法。   4. The reactor in the vapor phase growth apparatus according to claim 1, wherein the vapor phase growth apparatus is a vapor phase growth apparatus for forming a compound semiconductor that forms a compound semiconductor on a substrate. Gas replacement method. 前記気相成長装置は、MOCVD装置であることを特徴とする請求項4記載の気相成長装置における反応炉内のガス置換方法。   The method for gas replacement in a reaction furnace in a vapor phase growth apparatus according to claim 4, wherein the vapor phase growth apparatus is a MOCVD apparatus. 前記パージガスの積算供給量が前記反応炉の内容量よりも多く、かつ、前記反応炉内から排出される反応性ガスの濃度が許容濃度以下になるまで前記反応炉内のガスをパージガスに置換するガス置換操作を行うことを特徴とする請求項1乃至5のいずれか1項記載の気相成長装置における反応炉内のガス置換方法。   The purge gas replaces the gas in the reaction furnace until the integrated supply amount of the purge gas is larger than the internal volume of the reaction furnace and the concentration of the reactive gas discharged from the reaction furnace becomes equal to or lower than an allowable concentration. The gas replacement method in a reaction furnace in a vapor phase growth apparatus according to claim 1, wherein a gas replacement operation is performed.
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JP2012238772A (en) * 2011-05-13 2012-12-06 Sharp Corp Reaction chamber opening method and vapor phase growth device
JP2015146369A (en) * 2014-02-03 2015-08-13 大陽日酸株式会社 Lid opening method of reactor of vapor phase growth apparatus and vapor phase growth apparatus

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* Cited by examiner, † Cited by third party
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JP2010067686A (en) * 2008-09-09 2010-03-25 Hitachi Kokusai Electric Inc Method of manufacturing semiconductor device
JP2012238772A (en) * 2011-05-13 2012-12-06 Sharp Corp Reaction chamber opening method and vapor phase growth device
JP2015146369A (en) * 2014-02-03 2015-08-13 大陽日酸株式会社 Lid opening method of reactor of vapor phase growth apparatus and vapor phase growth apparatus

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