JP5037058B2 - Intermediate transfer chamber, substrate processing system, and exhaust method for intermediate transfer chamber - Google Patents

Intermediate transfer chamber, substrate processing system, and exhaust method for intermediate transfer chamber Download PDF

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JP5037058B2
JP5037058B2 JP2006210304A JP2006210304A JP5037058B2 JP 5037058 B2 JP5037058 B2 JP 5037058B2 JP 2006210304 A JP2006210304 A JP 2006210304A JP 2006210304 A JP2006210304 A JP 2006210304A JP 5037058 B2 JP5037058 B2 JP 5037058B2
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chamber
intermediate transfer
transfer chamber
gas
substrate
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JP2008041719A (en
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剛 守屋
博之 中山
圭祐 近藤
寛樹 岡
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Tokyo Electron Ltd
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Priority to US11/831,361 priority patent/US8113757B2/en
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • H01L21/67005Apparatus not specifically provided for elsewhere
    • H01L21/67011Apparatus for manufacture or treatment
    • H01L21/67155Apparatus for manufacturing or treating in a plurality of work-stations
    • H01L21/67201Apparatus for manufacturing or treating in a plurality of work-stations characterized by the construction of the load-lock chamber
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • H01L21/67005Apparatus not specifically provided for elsewhere
    • H01L21/67242Apparatus for monitoring, sorting or marking
    • H01L21/67276Production flow monitoring, e.g. for increasing throughput
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • H01L21/677Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations
    • H01L21/67739Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations into and out of processing chamber
    • H01L21/67742Mechanical parts of transfer devices
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/67Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
    • H01L21/677Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations
    • H01L21/67763Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere for conveying, e.g. between different workstations the wafers being stored in a carrier, involving loading and unloading
    • H01L21/67769Storage means

Description

本発明は、中間搬送室、基板処理システム、及び当該中間搬送室の排気方法に関し、特に、基板搬送時に真空排気する中間搬送室に関する。   The present invention relates to an intermediate transfer chamber, a substrate processing system, and an exhaust method for the intermediate transfer chamber, and more particularly to an intermediate transfer chamber that is evacuated during substrate transfer.

基板としてのウエハにプラズマ処理を施す基板処理システムは、ウエハを収容してプラズマ処理を施すプロセスモジュールと、該プロセスモジュールへウエハを搬入する中間搬送室としてのロード・ロックモジュールと、複数枚のウエハを収容する容器からウエハを取り出してロード・ロックモジュールに受け渡すローダーモジュールとを備える。   A substrate processing system that performs plasma processing on a wafer as a substrate includes a process module that accommodates the wafer and performs plasma processing, a load / lock module as an intermediate transfer chamber that carries the wafer into the process module, and a plurality of wafers And a loader module for taking out the wafer from the container for storing the wafer and delivering it to the load / lock module.

通常、基板処理システムのロード・ロックモジュールは、大気圧下でウエハを受け入れ、チャンバ内を所定の圧力まで真空排気した後、プロセスモジュール側のゲートを開いて、プロセスモジュール側にウエハを搬入し、プロセスが終了すると、プロセスモジュールからウエハを搬出し、プロセスモジュール側のゲートを閉めて、チャンバ内を大気圧に戻し、ウエハをローダーモジュールに搬出する、という機能を有する(例えば、特許文献1参照。)。   Usually, a load lock module of a substrate processing system receives a wafer under atmospheric pressure, evacuates the chamber to a predetermined pressure, opens a gate on the process module side, loads the wafer on the process module side, When the process is completed, the wafer is unloaded from the process module, the gate on the process module side is closed, the inside of the chamber is returned to atmospheric pressure, and the wafer is unloaded to the loader module (see, for example, Patent Document 1). ).

以前より、ロード・ロックモジュール内が真空排気される際に、チャンバ内にパーティクルが発生し、このパーティクルがウエハ表面に付着及び堆積し、ウエハプロセスにおいて当該パーティクルがウエハの欠陥となり、最終的に製造されるデバイスの歩留まりや、信頼性が低下するという問題があった。   When the load lock module is evacuated, particles are generated in the chamber, and these particles adhere to and accumulate on the wafer surface. In the wafer process, the particles become wafer defects, which are finally manufactured. There was a problem that the yield and reliability of the device to be used decreased.

真空排気時のチャンバ内におけるパーティクルの発生メカニズムとしては、従来より、チャンバ内に付着及び堆積しているパーティクルが真空排気時に巻き上げられ、それらがウエハに付着するという考え方が主流である。
特開2006−128578号公報
As a generation mechanism of particles in the chamber at the time of vacuum evacuation, conventionally, a concept that particles adhering and depositing in the chamber are wound up at the time of vacuum evacuation and adhere to the wafer is the mainstream.
JP 2006-128578 A

しかしながら、上述したパーティクルの発生メカニズムとは別に、チャンバ内に含まれる水分が真空排気時の内部ガスの断熱膨張による急激な温度低下により、凝固して、これに起因する微細パーティクルがウエハに付着するという現象も確認されるようになった。このパーティクルが付着したウエハにプロセスを施すと、例えば、花びら形状の腐食痕がウエハ上に残り、これがウエハの欠陥となる。   However, in addition to the particle generation mechanism described above, the moisture contained in the chamber solidifies due to a rapid temperature drop due to adiabatic expansion of the internal gas during evacuation and fine particles resulting from this adhere to the wafer. This phenomenon has also been confirmed. When the process is performed on the wafer to which the particles are adhered, for example, petal-shaped corrosion marks remain on the wafer, which becomes a defect of the wafer.

真空排気時の内部ガスの温度は、ガスの種類、チャンバ容積、及び排気速度等に大きく依存するが、数十℃ほど低下することが観測されている。チャンバ内に水分が含まれていると、ガス温度の急激な低下によって、小さなパーティクルを核に水分の凝結が生じ大きなパーティクルに成長し、温度によってはさらに氷に凝固し、それがウエハに付着する。この水分の凝結及び凝固という現象は、チャンバ内に核となるパーティクルがなくてもガス中の種々のイオンが凝結核となったり、水分子同士が凝集して大きく成長する等、チャンバ内に水分が含まれれば発生することがあり、深刻な問題を引き起こす。   It has been observed that the temperature of the internal gas during evacuation is reduced by several tens of degrees Celsius, although it largely depends on the type of gas, the chamber volume, the exhaust speed, and the like. If moisture is contained in the chamber, due to a rapid drop in gas temperature, moisture condenses from small particles to the core and grows into large particles, and depending on the temperature, it further solidifies into ice and adheres to the wafer. . This phenomenon of moisture condensation and coagulation is caused by the fact that various ions in the gas become condensation nuclei even when there are no core particles in the chamber, or water molecules agglomerate with each other and grow large. Can occur and cause serious problems.

本発明の目的は、基板の欠陥を防止することができる中間搬送室、基板処理システム、及び当該中間搬送室の排気方法を提供することにある。   The objective of this invention is providing the intermediate | middle conveyance chamber which can prevent the defect of a board | substrate, a substrate processing system, and the exhaust method of the said intermediate conveyance chamber.

上記目的を達成するために、請求項1記載の中間搬送室は、内部が第1の圧力で水分を含む第1の環境にある第1室と内部が第1の圧力よりも低い第2の圧力の第2の環境にある第2室との間に設けられ、当該第1室と当該第2室との間で双方向に基板を搬送し且つ当該基板を支持する支持部を有する搬送装置を備えた中間搬送室において、前記中間搬送室の内部圧力を前記第1の圧力から前記第2の圧力へ減圧すべく当該中間搬送室内を排気する排気装置と、該排気装置による排気の際に、前記支持部に支持された基板の直上のガスのコンダクタンスを制御するコンダクタンス制御装置とを備え、前記コンダクタンス制御装置は前記基板の主面と対向して設けられた平板状部材であり、且つ、前記平板状部材は加熱手段を備えず、前記排気装置による排気の際に前記平板状部材によって前記基板を加熱することなく前記基板の主面上において水分の凝結若しくは凝縮が生じないように、前記基板の主面と前記平板状部材との間隔を制御することによって前記基板の直上のガスのコンダクタンスを制御することを特徴とする。 In order to achieve the above object, the intermediate transfer chamber according to claim 1 includes a first chamber in a first environment containing water at a first pressure and a second chamber in which the interior is lower than the first pressure. A transfer device provided between a second chamber in a second environment of pressure and having a support unit that transfers the substrate bidirectionally between the first chamber and the second chamber and supports the substrate. And an exhaust device that exhausts the intermediate transport chamber to reduce the internal pressure of the intermediate transport chamber from the first pressure to the second pressure, and when exhausting by the exhaust device. , and a conductance control device which controls the conductance of the gas directly above the substrate supported by the supporting portion, the conductance control device is a plate-like member provided in the main surface facing the substrate, and , the flat member is not provided with heating means, the exhaust Device as condensation or condensation of moisture on the main surface of the substrate without heating the substrate with the flat plate-like member when the exhaust does not occur due to the main surface of the substrate and the distance between the flat member By controlling, the conductance of the gas immediately above the substrate is controlled.

請求項記載の中間搬送室は、請求項1記載の中間搬送室において、前記排気装置は前記基板の主面上の水分の凝結若しくは凝縮が生じない最大の排気速度で当該中間搬送室内の排気を行うことを特徴とする。 Intermediate chamber according to claim 2, wherein, in the intermediate conveying chamber according to claim 1 Symbol placement, the exhaust system of the intermediate transfer chamber at the maximum pumping speed condensation or condensation of moisture on the main surface of the substrate does not occur It is characterized by exhausting.

請求項記載の中間搬送室は、請求項記載の中間搬送室において、さらに、前記中間搬送室内の水分量を測定する水分量測定装置を備え、前記排気装置は当該水分量測定装置の測定結果に基づいて当該中間搬送室内の排気を行うことを特徴とする。 Intermediate chamber according to claim 3, wherein, in the intermediate conveying chamber according to claim 2, further comprising a water quantity measuring device for measuring the water content of the intermediate transfer chamber, the measurement of the exhaust system the water content measuring device Based on the result, exhaust in the intermediate transfer chamber is performed.

請求項記載の中間搬送室は、請求項又は記載の中間搬送室において、さらに、前記中間搬送室内の凝結若しくは凝縮した水分を検出する水分検出装置を備え、前記排気装置は当該水分検出装置の検出結果に基づいて当該中間搬送室内の排気を行うことを特徴とする。 The intermediate transfer chamber according to claim 4 is the intermediate transfer chamber according to claim 2 or 3 , further comprising a moisture detection device that detects condensed or condensed moisture in the intermediate transfer chamber, and the exhaust device includes the moisture detection device. Exhaust in the intermediate transfer chamber is performed based on the detection result of the apparatus.

請求項記載の中間搬送室は、請求項1乃至のいずれか1項に記載の中間搬送室において、さらに、前記中間搬送室内に乾燥したガスを供給する乾燥ガス供給装置を備えることを特徴とする。 The intermediate transfer chamber according to claim 5 is the intermediate transfer chamber according to any one of claims 1 to 4 , further comprising a dry gas supply device that supplies dry gas into the intermediate transfer chamber. And

請求項記載の中間搬送室は、請求項1乃至のいずれか1項に記載の中間搬送室において、さらに、前記中間搬送室内に所定の温度に加熱したガスを供給する加熱ガス供給装置を備えることを特徴とする。 The intermediate transfer chamber according to claim 6 is the intermediate transfer chamber according to any one of claims 1 to 5 , further comprising a heated gas supply device that supplies a gas heated to a predetermined temperature into the intermediate transfer chamber. It is characterized by providing.

請求項記載の中間搬送室は、請求項1乃至のいずれか1項に記載の中間搬送室において、さらに、前記中間搬送室内に該中間搬送室内を前記第1の圧力よりも高い圧力に昇圧するガスを供給する昇圧ガス供給装置を備えることを特徴とする。 Intermediate chamber according to claim 7, wherein, in the intermediate conveying chamber according to any one of claims 1 to 6, further an intermediate transfer chamber to a pressure higher than the first pressure to said intermediate transfer chamber A pressurization gas supply device that supplies a gas to be boosted is provided.

請求項記載の中間搬送室は、請求項1乃至のいずれか1項に記載の中間搬送室において、さらに、前記中間搬送室内に該中間搬送室内に含まれる水分を分解するガスを供給する水分分解ガス供給装置を備えることを特徴とする。 The intermediate transfer chamber according to claim 8 is the intermediate transfer chamber according to any one of claims 1 to 7 , further supplying a gas for decomposing moisture contained in the intermediate transfer chamber into the intermediate transfer chamber. A moisture decomposition gas supply device is provided.

請求項記載の中間搬送室は、請求項1乃至のいずれか1項に記載の中間搬送室において、さらに、前記中間搬送室における前記第1室との連通部において当該第1室内のガスの当該中間搬送室内への侵入を遮断するガスを噴出する遮断ガス噴出手段を備えることを特徴とする。 The intermediate transfer chamber according to claim 9 is the intermediate transfer chamber according to any one of claims 1 to 8 , further comprising a gas in the first chamber at a communication portion with the first chamber in the intermediate transfer chamber. Characterized in that it comprises a shut-off gas jetting means for jetting a gas that shuts out the intrusion into the intermediate transfer chamber.

請求項10記載の中間搬送室は、請求項1乃至のいずれか1項に記載の中間搬送室において、さらに、前記中間搬送室内及び内壁の少なくとも一部を冷却する冷却手段を備えることを特徴とする。 The intermediate transfer chamber according to claim 10 is the intermediate transfer chamber according to any one of claims 1 to 9 , further comprising cooling means for cooling at least a part of the intermediate transfer chamber and the inner wall. And

請求項11記載の中間搬送室は、請求項1乃至10のいずれか1項に記載の中間搬送室において、前記第1室内には乾燥したガスが供給されることを特徴とする。 Intermediate chamber according to claim 11, wherein, in the intermediate conveying chamber according to any one of claims 1 to 10, wherein the first chamber, characterized in that dry gas is supplied.

上記目的を達成するために、請求項12記載の基板処理システムは、前記第2室としての基板に処理を施す基板処理装置と、前記第1室としての前記基板を搬送する基板搬送装置と、請求項1乃至11のいずれか1項に記載の中間搬送室とを備えることを特徴とする。 In order to achieve the above object, a substrate processing system according to claim 12 , a substrate processing apparatus for processing a substrate as the second chamber, a substrate transfer apparatus for transferring the substrate as the first chamber , An intermediate transfer chamber according to any one of claims 1 to 11 is provided.

上記目的を達成するために、請求項13記載の中間搬送室の排気方法は、内部が第1の圧力で水分を含む第1の環境にある第1室と内部が第1の圧力よりも低い第2の圧力の第2の環境にある第2室との間に設けられ、当該第1室と当該第2室との間で双方向に基板を搬送し且つ当該基板を支持する支持部を有する搬送装置を備えた中間搬送室の排気方法において、前記中間搬送室の内部圧力を前記第1の圧力から前記第2の圧力へ減圧すべく当該中間搬送室内を排気する排気ステップと、該排気ステップによる排気の際に、前記支持部に支持された基板の直上のガスのコンダクタンスを制御するコンダクタンス制御ステップとを有し、前記コンダクタンス制御ステップでは、加熱手段を備えない平板状部材を前記基板の主面と対向するように配置し、前記平板状部材によって前記基板を加熱することなく、前記基板の主面上において水分の凝結若しくは凝縮が生じないように、前記基板の主面と前記平板状部材との間隔を制御することによって前記基板の直上のガスのコンダクタンスを制御することを特徴とする。 In order to achieve the above object, the method for exhausting the intermediate transfer chamber according to claim 13 is characterized in that the first chamber is in a first environment containing moisture at a first pressure and the interior is lower than the first pressure. A support unit provided between the second chamber in the second environment of the second pressure and configured to transport the substrate bidirectionally between the first chamber and the second chamber and support the substrate; An exhaust method for exhausting the intermediate transport chamber having the transport device, the exhaust step for exhausting the intermediate transport chamber to reduce the internal pressure of the intermediate transport chamber from the first pressure to the second pressure, A conductance control step for controlling the conductance of the gas immediately above the substrate supported by the support portion when evacuating by the step, and in the conductance control step, a flat plate member not provided with heating means is attached to the substrate. To face the main surface Arrangement, and without heating the substrate with the flat member, such condensation or condensation of moisture on the main surface of the substrate does not occur, to control the spacing of the main surface of the substrate and the flat plate-like member Thus, the conductance of the gas immediately above the substrate is controlled.

請求項1記載の中間搬送室、請求項13記載の中間搬送室の排気方法によれば、中間搬送室内の排気の際に、支持部に支持された基板の直上のガスのコンダクタンスを制御するので、基板の直上のガスの流れを緩やかにすることができる。その結果、基板直上のガスの断熱膨張を抑制することができるので、断熱膨張に起因するパーティクルが付着するのを防止することができ、もって、基板の欠陥を防止することができる。 According to the exhaust method of the intermediate transfer chamber according to claim 1 and the intermediate transfer chamber according to claim 13, the conductance of the gas immediately above the substrate supported by the support portion is controlled when the intermediate transfer chamber is exhausted. The gas flow immediately above the substrate can be made gentle. As a result, it is possible to suppress the adiabatic expansion of gas immediately above the substrate, can be particles due to adiabatic expansion is prevented from adhering, with, it is possible to prevent defects of the substrate.

また、請求項1記載の中間搬送室、請求項13記載の中間搬送室の排気方法によれば、
基板の主面と対向して加熱手段を備えない板状部材が設けられるので、基板の直上のガスのコンダクタンスを正確に制御することができ、基板の直上のガスの流れを確実に緩やかにすることができる。また、中間搬送室内の排気の際に、基板の直上のガス以外の中間搬送室内のガスでは断熱膨張により該ガス中の水分が凝固するが、基板の直上に板状部材が設けられるので、板状部材が基板のカバーの役割を果たす。したがって、基板に内部ガスの断熱膨張に起因するパーティクルが付着するのを確実に防止することができる。
According to the intermediate transfer chamber of claim 1 and the exhaust method of the intermediate transfer chamber of claim 13,
Since a plate-like member not provided with a heating means is provided opposite to the main surface of the substrate, the conductance of the gas immediately above the substrate can be accurately controlled, and the gas flow directly above the substrate is surely moderated. be able to. In addition, when exhausting in the intermediate transfer chamber, moisture in the intermediate transfer chamber other than the gas immediately above the substrate is solidified by adiabatic expansion, but a plate-like member is provided directly above the substrate. The shaped member serves as a cover for the substrate. Therefore, it is possible to reliably prevent the particles due to the adiabatic expansion of the internal gas from adhering to the substrate.

更に、請求項記載の中間搬送室、請求項13記載の中間搬送室の排気方法によれば、中間搬送室内の排気の際に、基板の主面上の水分の凝結若しくは凝縮が生じないように当該主面上のコンダクタンスを制御するので、基板に内部ガスの断熱膨張に起因するパーティクルが付着するのを適切に防止することができる。 Furthermore, an intermediate transfer chamber according to claim 1, according to the exhaust method of the intermediate conveyance chamber according to claim 13, wherein, when the evacuation of the intermediate transfer chamber, so that condensation or condensation of moisture on the main surface of the substrate does not occur In addition, since the conductance on the main surface is controlled, it is possible to appropriately prevent the particles due to the adiabatic expansion of the internal gas from adhering to the substrate.

請求項記載の中間搬送室によれば、基板の主面上の水分の凝結若しくは凝縮が生じない最大の排気速度で中間搬送室内の排気を行うので、内部ガスの断熱膨張に起因するパーティクルの発生を抑制しつつ、中間搬送室内のガスの圧力を効率よく低下させることができ、もって、内部ガスの断熱膨張による該ガス中の水分の凝固を適切に防止することができる。 According to the intermediate transfer chamber of the second aspect, since the exhaust in the intermediate transfer chamber is performed at the maximum exhaust speed at which moisture condensation or condensation on the main surface of the substrate does not occur, the particles caused by the adiabatic expansion of the internal gas While suppressing the generation, it is possible to efficiently reduce the pressure of the gas in the intermediate transfer chamber, and thus it is possible to appropriately prevent the solidification of moisture in the gas due to the adiabatic expansion of the internal gas.

請求項記載の中間搬送室によれば、中間搬送室内の水分量を測定し、水分量の測定結果に基づいて中間搬送室内の排気を行うので、中間搬送室内の水分量に応じて排気速度を適切に変更することができ、もって、中間搬送室内の水分の凝固を適切に防止することができる。 According to the intermediate transfer chamber of the third aspect, the moisture amount in the intermediate transfer chamber is measured and the intermediate transfer chamber is evacuated based on the measurement result of the moisture amount. Thus, it is possible to appropriately prevent moisture from solidifying in the intermediate transfer chamber.

請求項記載の中間搬送室によれば、中間搬送室内の凝結若しくは凝縮した水分を検出し、当該水分の検出結果に基づいて中間搬送室内の排気を行うので、中間搬送室内に発生した水分の検出結果に応じて排気速度を適切に変更することができ、もって、中間搬送室内の水分のさらなる凝固を適切に防止することができる。 According to the intermediate transfer chamber of claim 4, the condensed or condensed water in the intermediate transfer chamber is detected, and the intermediate transfer chamber is exhausted based on the detection result of the water. The exhaust speed can be appropriately changed according to the detection result, so that further solidification of moisture in the intermediate transfer chamber can be appropriately prevented.

請求項記載の中間搬送室によれば、中間搬送室内に乾燥したガスを供給するので、中間搬送室内のガスを水分を含んだガスから乾燥ガスに置換することができる。したがって、中間搬送室内のガス中に水分が含まれるのを抑制することができ、もって、当該ガス中の水分が断熱膨張により凝固するのをなくすことができる。 According to the intermediate transfer chamber of the fifth aspect , since the dried gas is supplied into the intermediate transfer chamber, the gas in the intermediate transfer chamber can be replaced with the dry gas from the moisture-containing gas. Therefore, it is possible to suppress moisture from being contained in the gas in the intermediate transfer chamber, so that moisture in the gas can be prevented from solidifying due to adiabatic expansion.

請求項記載の中間搬送室によれば、中間搬送室内に所定の温度に加熱したガスを供給するので、中間搬送室の内壁や基板の表面に付着した水分を蒸発させることができる。その結果、中間搬送室内のガス中に含まれる水分を除去することができ、もって、中間搬送室内のガス中に含まれる水分が断熱膨張により凝固するのをなくすことができる。また、中間搬送室内の排気の際における断熱膨張により中間搬送室内のガスの温度が水分の凝固点まで低下するのを防止することができる。したがって、当該ガス中に含まれる水分は凝固することがない。さらに、中間搬送室内のガスの温度を水分を含む大気の温度よりも高くすることができる。その結果、中間搬送室内に侵入する水分を含む大気を中間搬送室内の下部に流れ込ませることができ、水分を含む大気が基板の上方に回り込むのを防止することができる。したがって、基板の上方において水分が凝固するのを防止することができる。 According to the intermediate transfer chamber of the sixth aspect, since the gas heated to a predetermined temperature is supplied into the intermediate transfer chamber, the water adhering to the inner wall of the intermediate transfer chamber and the surface of the substrate can be evaporated. As a result, it is possible to remove moisture contained in the gas in the intermediate transfer chamber, thereby eliminating the moisture contained in the gas in the intermediate transfer chamber from solidifying due to adiabatic expansion. In addition, it is possible to prevent the temperature of the gas in the intermediate transfer chamber from being lowered to the freezing point of moisture due to adiabatic expansion during exhaust in the intermediate transfer chamber. Therefore, the moisture contained in the gas does not solidify. Furthermore, the temperature of the gas in the intermediate transfer chamber can be made higher than the temperature of the atmosphere containing moisture. As a result, the atmosphere containing moisture entering the intermediate transfer chamber can flow into the lower portion of the intermediate transfer chamber, and the atmosphere containing moisture can be prevented from flowing upward above the substrate. Therefore, it is possible to prevent moisture from solidifying above the substrate.

請求項記載の中間搬送室によれば、中間搬送室内に中間搬送室内を第1の圧力よりも高い圧力に昇圧するガスを供給するので、中間搬送室内のガスの圧力を水分を含む大気の圧力よりも高くすることができる。その結果、水分を含む大気が中間搬送室内に流れ込むのを防ぐことができ、もって、中間搬送室内に水分を含んだ大気が供給されるのを防止することができる。 According to the intermediate transfer chamber of the seventh aspect, the gas for raising the pressure in the intermediate transfer chamber to a pressure higher than the first pressure is supplied to the intermediate transfer chamber. It can be higher than the pressure. As a result, it is possible to prevent the moisture-containing air from flowing into the intermediate transfer chamber, and thus it is possible to prevent the moisture-containing air from being supplied into the intermediate transfer chamber.

請求項記載の中間搬送室によれば、中間搬送室内に中間搬送室内に含まれる水分を分解するガスを供給するので、中間搬送室内のガス中に含まれる水分を分解することができる。その結果、中間搬送室内のガス中に水分が存在するのを防止することができ、もって、当該ガス中の水分が断熱膨張により凝固するのをなくすことができる。 According to the intermediate transfer chamber of the eighth aspect, since the gas for decomposing the moisture contained in the intermediate transfer chamber is supplied into the intermediate transfer chamber, the moisture contained in the gas in the intermediate transfer chamber can be decomposed. As a result, it is possible to prevent moisture from being present in the gas in the intermediate transfer chamber, and thus to prevent the moisture in the gas from solidifying due to adiabatic expansion.

請求項記載の中間搬送室によれば、中間搬送室における第1室との連通部において第1室内のガスの中間搬送室内への侵入を遮断するガスを噴出するので、水分を含む大気が中間搬送室内に侵入するのを遮断することができる。したがって、中間搬送室内に水分を含んだ大気が供給されることを防止することができる。 According to the intermediate transfer chamber according to claim 9, since discharges gas to block the entry of the communication portion between the first chamber in the intermediate chamber to the intermediate conveying chamber of the first chamber of a gas, the atmosphere containing moisture Intrusion into the intermediate transfer chamber can be blocked. Therefore, it is possible to prevent the atmosphere containing moisture from being supplied into the intermediate transfer chamber.

請求項10記載の中間搬送室によれば、中間搬送室内及び内壁の少なくとも一部を冷却するので、中間搬送室内のガス中の水分を凝固させ、当該ガス中の水分の割合を低下させることができ、もって、ガス中の水分が断熱膨張により凝固することを防止することができる。 According to the intermediate transfer chamber of claim 10, since at least a part of the intermediate transfer chamber and the inner wall is cooled, the moisture in the gas in the intermediate transfer chamber is solidified, and the ratio of the moisture in the gas can be reduced. Therefore, it is possible to prevent moisture in the gas from solidifying due to adiabatic expansion.

請求項11記載の中間搬送室によれば、第1室内に乾燥したガスが供給されるので、第1室内のガスを水分を含んだ大気から乾燥ガスに置換することができる。その結果、第1室内から中間搬送室内に水分を含んだ大気が流れ込むのを防ぐことができ、もって、中間搬送室内に水分を含んだ大気が供給されるのを防止することができる。 According to the intermediate transfer chamber of the eleventh aspect , since the dried gas is supplied into the first chamber, the gas in the first chamber can be replaced with dry gas from the atmosphere containing moisture. As a result, it is possible to prevent the moisture-containing atmosphere from flowing into the intermediate transfer chamber from the first chamber, and it is therefore possible to prevent the moisture-containing atmosphere from being supplied into the intermediate transfer chamber.

請求項12記載の基板処理システムによれば、請求項1乃至11のいずれか1項に記載の中間搬送室を備えるので、基板の欠陥を防止することができる。 According to the substrate processing system of the twelfth aspect, since the intermediate transfer chamber according to any one of the first to eleventh aspects is provided, defects of the substrate can be prevented.

以下、本発明の実施の形態について図面を参照しながら説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

まず、本発明の実施の形態に係る基板処理システムについて説明する。   First, a substrate processing system according to an embodiment of the present invention will be described.

図1は、本発明の実施の形態に係る基板処理システムの概略構成を示す断面図である。   FIG. 1 is a cross-sectional view showing a schematic configuration of a substrate processing system according to an embodiment of the present invention.

図1において、基板処理システム1は、基板としての半導体ウエハ(以下、単に「ウエハ」という。)WにRIE(Reactive Ion Etching)処理やアッシング処理等のプラズマ処理を施すプロセスモジュール(Process Module)(以下、「P/M」という。)2と、ウエハWを収容する容器としてのフープ(Front Opening Unified Pod)5からウエハWを取り出す大気系搬送装置3と、該大気系搬送装置3及びP/M2の間に配置され、大気系搬送装置3からP/M2、若しくはP/M2から大気系搬送装置3へウエハWを搬出入する中間搬送室としてのロード・ロックモジュール(Load-Lock Module)(以下、「LL/M」という。)4とを備える。   In FIG. 1, a substrate processing system 1 is a process module (Process Module) that performs plasma processing such as RIE (Reactive Ion Etching) processing and ashing processing on a semiconductor wafer (hereinafter simply referred to as “wafer”) W as a substrate. (Hereinafter referred to as “P / M”) 2, an atmospheric transfer device 3 that takes out the wafer W from a FOUP (Front Opening Unified Pod) 5 as a container for containing the wafer W, and the atmospheric transfer device 3 and the P / M Load-Lock Module (Load-Lock Module) as an intermediate transfer chamber which is arranged between M2 and carries wafer W to / from P / M2 from the atmospheric transfer device 3 or from the P / M2 to the atmospheric transfer device 3. (Hereinafter referred to as “LL / M”) 4.

P/M2及びLL/M4の内部は真空引き可能に構成され、大気系搬送装置3の内部は常時大気圧に維持される。また、P/M2及びLL/M4、並びにLL/M4及び大気系搬送装置3は夫々ゲートバルブ6,7によって接続される。該ゲートバルブ6,7は開閉自在であり、P/M2及びLL/M4、並びにLL/M4及び大気系搬送装置3の間を連通し、若しくは遮断する。   The insides of P / M2 and LL / M4 are configured to be evacuated, and the inside of the atmospheric transfer device 3 is always maintained at atmospheric pressure. Further, P / M2 and LL / M4, and LL / M4 and the atmospheric transfer device 3 are connected by gate valves 6 and 7, respectively. The gate valves 6 and 7 are openable and closable, and communicate or block between P / M2 and LL / M4 and between LL / M4 and the atmospheric transfer device 3.

大気系搬送装置3は、フープ5を載置するフープ載置台50と、ローダーモジュール(Loader Module)(以下、「L/M」という。)51(第1室)と、該L/M51内にガスを供給するガス供給系60とを有する。   The atmospheric transfer device 3 includes a hoop mounting table 50 on which the hoop 5 is mounted, a loader module (hereinafter referred to as “L / M”) 51 (first chamber), and the L / M 51. And a gas supply system 60 for supplying gas.

フープ載置台50は上面が平面を呈する台状物であり、フープ5は、例えば、25枚のウエハWを等ピッチで多段に載置して収容する。また、L/M51は、直方体状の箱状物であり、内部においてウエハWを搬送するスカラタイプの搬送アーム52を有する。   The hoop mounting table 50 is a trapezoid whose upper surface has a flat surface, and the hoop 5 stores, for example, 25 wafers W placed in multiple stages at an equal pitch. The L / M 51 is a rectangular parallelepiped box-like object, and has a scalar type transfer arm 52 that transfers the wafer W therein.

また、L/M51のフープ載置台50側の側面には、該フープ載置台50に載置されたフープ5に対向してフープオープナー(図示しない)が設けられる。該フープオープナーはフープ5の前面扉を開きフープ5とL/M51の内部を連通させる。   Further, a hoop opener (not shown) is provided on the side surface of the L / M 51 on the side of the hoop mounting table 50 so as to face the hoop 5 mounted on the hoop mounting table 50. The hoop opener opens the front door of the hoop 5 so that the hoop 5 communicates with the inside of the L / M 51.

搬送アーム52は、屈伸可能に構成された多関節状の搬送アーム腕部53と、該搬送アーム腕部53の先端に取り付けられたピック54とを有し、該ピック54はウエハWを直接的に載置するように構成されている。また、搬送アーム52は、屈伸可能に構成された多関節腕状のマッピングアーム55を有しており、該マッピングアーム55の先端には、例えば、レーザ光を発してウエハWの有無を確認するマッピングセンサ(図示しない)が配置されている。これらの搬送アーム腕部53とマッピングアーム55との各基端は、搬送アーム52の基部56から立設されたアーム基端部支柱57に沿って昇降する昇降台58に連結されている。また、当該アーム基端部支柱57は旋回可能に構成されている。フープ5に収容されているウエハWの位置及び数を認識するために行うマッピング操作では、マッピングアーム55が延伸された状態で、該マッピングアーム55が上昇或いは下降することにより、フープ5内におけるウエハWの位置及び枚数を確認する。   The transfer arm 52 includes an articulated transfer arm arm portion 53 configured to bend and stretch, and a pick 54 attached to the tip of the transfer arm arm portion 53. It is comprised so that it may mount. The transfer arm 52 has an articulated arm-like mapping arm 55 configured to be able to bend and stretch. For example, a laser beam is emitted to the tip of the mapping arm 55 to check the presence or absence of the wafer W. A mapping sensor (not shown) is arranged. The base ends of the transfer arm arm portion 53 and the mapping arm 55 are connected to a lift 58 that moves up and down along an arm base end support column 57 erected from the base portion 56 of the transfer arm 52. The arm base end support column 57 is configured to be turnable. In the mapping operation performed for recognizing the position and number of the wafers W accommodated in the hoop 5, the mapping arm 55 is lifted or lowered while the mapping arm 55 is extended, whereby the wafer in the hoop 5. Check the position and number of W.

搬送アーム52は、搬送アーム腕部53によって屈曲自在であり、アーム基端部支柱57によって旋回自在であるため、ピック54に載置したウエハWを、フープ5及びLL/M4の間において自在に搬送することができる。   Since the transfer arm 52 can be bent by the transfer arm arm portion 53 and can be turned by the arm base end support column 57, the wafer W placed on the pick 54 can be freely placed between the hoop 5 and the LL / M4. Can be transported.

ガス供給系60は、L/M51の外部からL/M51の内部へ貫通したガス導入管61と、該ガス導入管61のL/M51外部側先端に接続されたガス供給装置(図示しない)と、ガス導入管61においてL/M51及びガス供給装置の間に配置された制御バルブ63とを有する。本実施の形態において、ガス供給系60は、L/M51内にNガスやドライエア等の乾燥ガスを供給し、L/M51内の水分量を減少させる。 The gas supply system 60 includes a gas introduction pipe 61 penetrating from the outside of the L / M 51 into the L / M 51, and a gas supply device (not shown) connected to the L / M 51 outside tip of the gas introduction pipe 61. The gas introduction pipe 61 has a control valve 63 disposed between the L / M 51 and the gas supply device. In the present embodiment, the gas supply system 60 supplies a dry gas such as N 2 gas or dry air into the L / M 51 to reduce the amount of water in the L / M 51.

LL/M4は、屈伸及び旋回自在になされた移載アーム70(搬送装置)が配置されると共に、移載アーム70の後述するピック74のウエハ載置面の直上に対向して設けられた板状部材90(コンダクタンス制御装置)を有するチャンバ71と、該チャンバ71内にガスを供給するガス供給系72と、チャンバ71内を排気するLL/M排気系73(排気装置)とを有する。   The LL / M4 is provided with a transfer arm 70 (conveying device) which can be bent and stretched and pivoted, and a plate provided opposite to a wafer mounting surface of a pick 74 (to be described later) of the transfer arm 70. A chamber 71 having a cylindrical member 90 (conductance control device), a gas supply system 72 for supplying gas into the chamber 71, and an LL / M exhaust system 73 (exhaust device) for exhausting the chamber 71.

移載アーム70は複数の腕部からなるスカラタイプの搬送アームであり、その先端に取り付けられたピック74(支持部)を有する。該ピック74はウエハWを直接的に載置するように構成される。なお、ピック74の形状は上述したピック54の形状と略同様である。   The transfer arm 70 is a SCARA-type transfer arm composed of a plurality of arm portions, and has a pick 74 (support portion) attached to the tip thereof. The pick 74 is configured to directly place the wafer W thereon. The shape of the pick 74 is substantially the same as the shape of the pick 54 described above.

ウエハWが大気系搬送装置3からP/M2へ搬入される場合、ゲートバルブ7が開放されたとき、移載アーム70はL/M51内の搬送アーム52からウエハWを受け取り、ゲートバルブ6が開放されたとき、移載アーム70はP/M2のチャンバ10(第2室)内へ進入し、載置台12の上面から突出したプッシャーピン(図示しない)の上端にウエハWを載置する。また、ウエハWがP/M2から大気系搬送装置3へ搬入される場合、ゲートバルブ6が開放されたとき、移載アーム70はP/M2のチャンバ10内へ進入し、載置台12の上面から突出したプッシャーピンの上端に載置されたウエハWを受け取る。ゲートバルブ7が開放されたとき、移載アーム70はL/M51内の搬送アーム52へウエハWを受け渡す。なお、移載アーム70は、スカラタイプに限られず、フロッグレッグタイプやダブルアームタイプであってもよい。   When the wafer W is carried into the P / M 2 from the atmospheric transfer device 3, when the gate valve 7 is opened, the transfer arm 70 receives the wafer W from the transfer arm 52 in the L / M 51, and the gate valve 6 When opened, the transfer arm 70 enters the P / M2 chamber 10 (second chamber) and places the wafer W on the upper end of a pusher pin (not shown) protruding from the upper surface of the mounting table 12. When the wafer W is transferred from the P / M 2 to the atmospheric transfer device 3, the transfer arm 70 enters the P / M 2 chamber 10 when the gate valve 6 is opened, and the upper surface of the mounting table 12. The wafer W placed on the upper end of the pusher pin projecting from is received. When the gate valve 7 is opened, the transfer arm 70 delivers the wafer W to the transfer arm 52 in the L / M 51. The transfer arm 70 is not limited to the scalar type, and may be a frog leg type or a double arm type.

ガス供給系72は、チャンバ71の外部からチャンバ71の内部へ貫通するガス導入管75と、ガス導入管75のチャンバ71外部側先端に接続されたガス供給装置(図示しない)と、ガス導入管75においてチャンバ71及びガス供給装置の間に配置された制御バルブ77と、ガス導入管75においてチャンバ71及び制御バルブ77の間に配置されたヒーティングユニット76と、ガス導入管75のチャンバ71内部側先端に配置されたガスを噴出するガス供給口を有する。本実施の形態においては、ガス供給口の先端に一対のブレークフィルタ(Break Filter)80を有する。本実施の形態において、ガス供給系72は、チャンバ71内に不活性ガス、Nガスやドライエア等の乾燥ガス、ヒーティングユニット76により所定の温度以上に加熱したガス、若しくは後述する水分を分解するガスを供給する。ブレークフィルタ80は、その長さが、例えば200mmに設定された多孔質状のセラミックス製フィルタである。 The gas supply system 72 includes a gas introduction pipe 75 penetrating from the outside of the chamber 71 to the inside of the chamber 71, a gas supply apparatus (not shown) connected to the front end of the gas introduction pipe 75 on the outside of the chamber 71, and a gas introduction pipe 75, a control valve 77 disposed between the chamber 71 and the gas supply device, a heating unit 76 disposed between the chamber 71 and the control valve 77 in the gas introduction pipe 75, and the interior of the chamber 71 of the gas introduction pipe 75. It has a gas supply port for ejecting gas arranged at the side tip. In the present embodiment, a pair of break filters 80 is provided at the tip of the gas supply port. In the present embodiment, the gas supply system 72 decomposes an inert gas, a dry gas such as N 2 gas or dry air, a gas heated to a predetermined temperature or higher by the heating unit 76, or moisture described later in the chamber 71. Supply the gas. The break filter 80 is a porous ceramic filter whose length is set to 200 mm, for example.

LL/M排気系73は、チャンバ71の内部へ貫通する排気管78と、該排気管78の途中に配置された制御バルブ79とを有し、上述したガス供給系72と協働してチャンバ71の内部の圧力を制御する。   The LL / M exhaust system 73 includes an exhaust pipe 78 penetrating into the chamber 71 and a control valve 79 disposed in the middle of the exhaust pipe 78, and cooperates with the gas supply system 72 described above to form a chamber. The pressure inside 71 is controlled.

次に、図1におけるLL/M4において実行される真空排気処理について説明する。   Next, the vacuum evacuation process executed in LL / M4 in FIG. 1 will be described.

真空排気処理が行なわれる際のウエハWの搬送手順としては、まず、フープ5内に収容されたウエハWを搬送アーム52により大気圧下のLL/M4のチャンバ71内に搬入し、ゲートバルブ7を閉じてからLL/M排気系73によりチャンバ71内を真空排気し、チャンバ71内が所定の圧力になるとゲートバルブ6を開いて移載アーム70によりウエハWをP/M2のチャンバ10内に搬送する。   As a transfer procedure of the wafer W when the vacuum evacuation process is performed, first, the wafer W accommodated in the FOUP 5 is loaded into the LL / M4 chamber 71 under the atmospheric pressure by the transfer arm 52, and the gate valve 7 , The chamber 71 is evacuated by the LL / M exhaust system 73, and when the chamber 71 reaches a predetermined pressure, the gate valve 6 is opened and the transfer arm 70 moves the wafer W into the P / M 2 chamber 10. Transport.

従来から、ウエハWの搬送時のLL/M4のチャンバ71内における真空排気の過程で、チャンバ71内のガスが断熱膨張により急速に冷却され、チャンバ71内のガスに含まれる水分が凝固して、これに起因する微細パーティクルがウエハWに付着するという問題が発生していた。   Conventionally, in the process of evacuation in the chamber 71 of the LL / M4 during the transfer of the wafer W, the gas in the chamber 71 is rapidly cooled by adiabatic expansion, and moisture contained in the gas in the chamber 71 is solidified. There has been a problem that fine particles resulting from this adhere to the wafer W.

本実施の形態においては、図2に示すように、移載アーム70のピック74のウエハ載置面の直上に対向して板状部材90を設け、ピック74のウエハ載置面に載置されたウエハWの直上におけるガスの流れのコンダクタンスを小さくする。これにより、LL/M排気系73による真空排気の際に、ウエハWの直上のガスの流れを緩やかにすることができ、もって、当該ガスの断熱膨張による該ガス中の水分の凝固を防止することができる。また、LL/M排気系73による真空排気の際に、上記ウエハWの直上のガス以外のチャンバ71内のガスは断熱膨張により該ガス中の水分が凝固するが、ウエハWの直上に板状部材90が設けられているため、板状部材90がウエハWのカバーの役割を果たし、もって、ウエハWに上記ガス中の水分が凝固して発生したパーティクルが付着することがない。   In the present embodiment, as shown in FIG. 2, a plate-like member 90 is provided directly above the wafer placement surface of the pick 74 of the transfer arm 70 and placed on the wafer placement surface of the pick 74. The conductance of the gas flow immediately above the wafer W is reduced. As a result, during the vacuum evacuation by the LL / M evacuation system 73, the flow of the gas immediately above the wafer W can be moderated, thereby preventing the moisture in the gas from solidifying due to the adiabatic expansion of the gas. be able to. Further, when the LL / M exhaust system 73 is evacuated, the gas in the chamber 71 other than the gas directly above the wafer W solidifies due to adiabatic expansion, and the moisture in the gas is solidified. Since the member 90 is provided, the plate-like member 90 serves as a cover for the wafer W, so that particles generated by the solidification of moisture in the gas do not adhere to the wafer W.

なお、ガス中の水分の凝固を防止するためには、ガスの排気速度を3.8l/secまで低下させればよいことが本発明者によって確認されており、該排気速度に相当するウエハW直上のコンダクタンスは46.3l/secである。ここで、チャンバ71のガスの流れ方向に沿う長さ(図2中における水平方向の長さ)を379mmとし、チャンバ71のガスの流れ方向に直角な方向に沿う長さ(図2中における奥行き方向の長さ)を309mmとすると、上述したコンダクタンスを実現するためには、ピック74のウエハ載置面に載置されたウエハWと板状部材90との間の距離を10.7mmに設定するのがよい。   It has been confirmed by the present inventor that the gas exhaust speed should be reduced to 3.8 l / sec in order to prevent the moisture in the gas from solidifying, and the wafer W corresponding to the exhaust speed is confirmed. The direct conductance is 46.3 l / sec. Here, the length of the chamber 71 along the gas flow direction (horizontal length in FIG. 2) is 379 mm, and the length along the direction perpendicular to the gas flow direction of the chamber 71 (depth in FIG. 2). If the length in the direction is 309 mm, the distance between the wafer W placed on the wafer placement surface of the pick 74 and the plate member 90 is set to 10.7 mm in order to realize the above-described conductance. It is good to do.

本実施の形態によれば、ピック74のウエハ載置面に載置されたウエハWの直上におけるガスの流れのコンダクタンスを制御する板状部材90が、ウエハWの直上のガスの流れを緩やかにするので、LL/M4のチャンバ71内における真空排気の過程において、ウエハWに内部ガスの断熱膨張に起因するパーティクルが付着するのを防止することができ、もって、ウエハWの欠陥を防止することができる。   According to the present embodiment, the plate-like member 90 that controls the conductance of the gas flow immediately above the wafer W placed on the wafer placement surface of the pick 74 makes the gas flow just above the wafer W gentle. Therefore, in the process of evacuation in the chamber 71 of the LL / M4, it is possible to prevent the particles due to the adiabatic expansion of the internal gas from adhering to the wafer W, thereby preventing defects in the wafer W. Can do.

また、本実施の形態では、ピック74のウエハ載置面の直上に対向して板状部材90を設け、ピック74のウエハ載置面に載置されたウエハWの直上のコンダクタンスを小さくしているが、板状部材90を設けることなく、ピック74のウエハ載置面に載置されたウエハWを持ち上げることにより、チャンバ71内の天井に当該ウエハを接近させ、当該ウエハの直上のコンダクタンスを小さくしてもよい。   In the present embodiment, a plate-like member 90 is provided directly above the wafer mounting surface of the pick 74 to reduce the conductance immediately above the wafer W mounted on the wafer mounting surface of the pick 74. However, by lifting the wafer W placed on the wafer placement surface of the pick 74 without providing the plate-like member 90, the wafer is brought close to the ceiling in the chamber 71, and the conductance immediately above the wafer is increased. It may be small.

また、本実施の形態において、LL/M排気系73によるチャンバ71内の真空排気の排気速度を制御して、スロー排気を行ってもよく、これにより、チャンバ71内のガスの圧力を緩やかに低下させることができ、もって、当該ガスの断熱膨張による該ガス中の水分の凝固を防止することができる。   Further, in the present embodiment, the evacuation speed of the vacuum exhaust in the chamber 71 by the LL / M exhaust system 73 may be controlled to perform the slow exhaust, thereby gradually reducing the pressure of the gas in the chamber 71. Therefore, it is possible to prevent the moisture in the gas from solidifying due to the adiabatic expansion of the gas.

また、本実施の形態において、図3(A)に示すように、チャンバ71内に湿度計91を設け、湿度計91を用いてチャンバ71内の水分量を測定し、この測定結果に基づいてLL/M排気系73によるチャンバ71内の真空排気の排気速度を動的に制御してもよく、これにより、チャンバ71内の水分量に応じて排気速度を適切に変更することができ、もって、当該チャンバ71内の水分の凝固を適切に防止することができる。   Further, in the present embodiment, as shown in FIG. 3A, a hygrometer 91 is provided in the chamber 71, the moisture content in the chamber 71 is measured using the hygrometer 91, and based on the measurement result. The evacuation speed of the vacuum exhaust in the chamber 71 by the LL / M exhaust system 73 may be dynamically controlled, whereby the exhaust speed can be appropriately changed according to the amount of water in the chamber 71, The moisture in the chamber 71 can be appropriately prevented from solidifying.

また、本実施の形態において、図3(A)に示すように、チャンバ71内にパーティクルモニタ92aを設け、パーティクルモニタ92aを用いてチャンバ71内のガスの断熱膨張に起因して発生したパーティクルを検出し、この検出結果に基づいてLL/M排気系73によるチャンバ71内の真空排気の排気速度を動的に制御してもよく、これにより、チャンバ71内に発生したパーティクルの検出結果に応じて排気速度を適切に変更することができ、もって、当該チャンバ71内の水分の凝固を適切に防止することができる。本実施の形態においては、図3(A)に示すように、パーティクルモニタ92bをチャンバ71内のLL/M排気系73の排気ラインに設け、排気パーティクルを検出し、排気パーティクルの検出結果に応じてLL/M排気系73によるチャンバ71内の真空排気の排気速度を動的に制御してもよい。なお、パーティクルモニタ92a,92bはレーザ光散乱法等を用いてパーティクルを検出する。   Further, in this embodiment, as shown in FIG. 3A, a particle monitor 92a is provided in the chamber 71, and particles generated due to adiabatic expansion of gas in the chamber 71 are detected using the particle monitor 92a. The evacuation speed of the vacuum exhaust in the chamber 71 by the LL / M exhaust system 73 may be dynamically controlled based on the detection result, and according to the detection result of the particles generated in the chamber 71. Thus, it is possible to appropriately change the exhaust speed, and thus it is possible to appropriately prevent the moisture in the chamber 71 from solidifying. In the present embodiment, as shown in FIG. 3A, a particle monitor 92b is provided in the exhaust line of the LL / M exhaust system 73 in the chamber 71 to detect exhaust particles, and according to the detection result of the exhaust particles. Thus, the exhaust speed of the vacuum exhaust in the chamber 71 by the LL / M exhaust system 73 may be dynamically controlled. The particle monitors 92a and 92b detect particles using a laser light scattering method or the like.

また、本実施の形態において、図3(B)に示すように、チャンバ71内に該チャンバ71内のガスと接触する冷却体等を備えた冷却装置93を設け、チャンバ71内のガス中の水分を冷却装置93にて凝固し、当該ガス中の水分の割合を低下させてもよく、これにより、LL/M排気系73によりチャンバ71内を真空排気する際に、チャンバ71内のガス中に含まれる水分の割合を低くすることができ、当該ガス中の水分が断熱膨張により凝固することを防止することができる。本実施の形態においては、チャンバ71内に冷却装置93を設け、チャンバ71内のガス中の水分の割合を低下させているが、冷却装置93を設けることなく、チャンバ71内及び内壁の少なくとも一部を水分が凝固する温度に冷却することにより、チャンバ71内のガス中の水分の割合を低下させてもよい。   Further, in the present embodiment, as shown in FIG. 3B, a cooling device 93 including a cooling body or the like in contact with the gas in the chamber 71 is provided in the chamber 71, The moisture may be solidified by the cooling device 93 and the ratio of the moisture in the gas may be reduced. As a result, when the chamber 71 is evacuated by the LL / M exhaust system 73, The proportion of moisture contained in the gas can be reduced, and moisture in the gas can be prevented from solidifying due to adiabatic expansion. In the present embodiment, the cooling device 93 is provided in the chamber 71 to reduce the ratio of moisture in the gas in the chamber 71. However, at least one of the inside of the chamber 71 and the inner wall is not provided without providing the cooling device 93. The proportion of moisture in the gas in the chamber 71 may be reduced by cooling the part to a temperature at which moisture solidifies.

また、本実施の形態において、図3(C)に示すように、チャンバ71のゲートバルブ7との連通部においてガス噴出系94を備え、ガス噴出系94によりゲートバルブ7が開いた際にL/M51内の水分を含む大気がチャンバ71内に侵入するのを遮断すべくゲートバルブ7の近傍においてカーテン状流れのガスを噴出してもよく、これにより、チャンバ71内にL/M51内から水分を含む大気の侵入を防ぐことができ、もって、チャンバ71内に水分を含んだ大気が供給されることを防止することができる。   Further, in the present embodiment, as shown in FIG. 3C, a gas ejection system 94 is provided at the communication portion of the chamber 71 with the gate valve 7, and when the gate valve 7 is opened by the gas ejection system 94, L In order to block the atmosphere containing moisture in the / M51 from entering the chamber 71, a gas in the form of a curtain may be ejected in the vicinity of the gate valve 7 so that the chamber 71 can enter the chamber 71 from within the L / M51. Invasion of the atmosphere containing moisture can be prevented, so that the atmosphere containing moisture can be prevented from being supplied into the chamber 71.

また、本実施の形態において、図4(A)に示すように、ガス供給系72によりチャンバ71内にNガスやドライエア等の乾燥ガスを供給し、チャンバ71内のガスを水分を含んだガスから当該乾燥ガスに置換してもよく、これにより、LL/M排気系73によりチャンバ71内を真空排気する際に、チャンバ71内のガス中に水分が含まれるのを抑制することができ、当該ガス中の水分が断熱膨張により凝固するのをなくすことができる。 Further, in the present embodiment, as shown in FIG. 4A, a dry gas such as N 2 gas or dry air is supplied into the chamber 71 by the gas supply system 72, and the gas in the chamber 71 contains moisture. The gas may be replaced with the dry gas, and thereby, when the inside of the chamber 71 is evacuated by the LL / M exhaust system 73, the moisture in the gas in the chamber 71 can be suppressed. The moisture in the gas can be prevented from solidifying due to adiabatic expansion.

また、本実施の形態において、図4(A)に示すように、ガス供給系72によりチャンバ71内に水分を分解するガスを供給し、チャンバ71内のガス中に含まれる水分を分解してもよく、これにより、LL/M排気系73によりチャンバ71内を真空排気する際に、チャンバ71内のガス中に水分が存在するのを防止することができ、当該ガス中の水分が断熱膨張により凝固するのをなくすことができる。水分を分解するガスの供給方法は任意であるが、単調に供給することに限らず、例えば、効率よく水分を分解するためにパルス化して供給、若しくは脈動を加えて圧力を変動させながら供給してもよい。これにより、水分を分解するガスと水分を含むガスとの混合を促進して水分の分解をより効率よく行うことができる。   Further, in this embodiment, as shown in FIG. 4A, a gas supply system 72 supplies a gas for decomposing moisture into the chamber 71, and decomposes moisture contained in the gas in the chamber 71. As a result, when the inside of the chamber 71 is evacuated by the LL / M exhaust system 73, it is possible to prevent the presence of moisture in the gas in the chamber 71, and the moisture in the gas is adiabatically expanded. It is possible to eliminate coagulation. The gas supply method for decomposing moisture is arbitrary, but is not limited to monotonous supply. For example, it is supplied by pulsing to efficiently decompose moisture, or by supplying pressure while fluctuating the pressure. May be. Thereby, mixing of the gas which decomposes | disassembles a water | moisture content and the gas containing a water | moisture content is accelerated | stimulated, and a water | moisture content can be decomposed | disassembled more efficiently.

水分を分解するガスは、オキシハロゲン類等であり、例えば、メチルシラン化合物、ジクロロプロパン、ジブロモプロパン、ニトロシルクロライド、カルボシルクロライド、カルボシルフロライド、シボラン、塩素、フッ素、チオニルブロマイド、ヨウドメチルプロパン、アセチルクロライド、アセトンジアチルアセタル、一酸化炭素である。メチルシラン化合物は、トリメチルクロロシラン、ジメチルジクロロシラン、モノメチルトリクロロシラン、テトラクロロシラン等である。   Gases for decomposing moisture are oxyhalogens and the like, for example, methylsilane compounds, dichloropropane, dibromopropane, nitrosyl chloride, carbosyl chloride, carbosyl fluoride, siborane, chlorine, fluorine, thionyl bromide, iodomethylpropane, Acetyl chloride, acetone diacyl acetal, carbon monoxide. Examples of the methylsilane compound include trimethylchlorosilane, dimethyldichlorosilane, monomethyltrichlorosilane, and tetrachlorosilane.

また、本実施の形態において、図4(B)に示すように、ガス供給系72によりチャンバ71内に100℃以上に加熱したガスを供給し、チャンバ71の内壁やウエハWの表面に付着した水分を蒸発させてもよく、これにより、チャンバ71内のガス中に含まれる水分を除去することができ、もって、LL/M排気系73によりチャンバ71内を真空排気する際に、チャンバ71内のガス中に含まれる水分が断熱膨張により凝固するのをなくすことができる。   In this embodiment, as shown in FIG. 4B, a gas heated to 100 ° C. or higher is supplied into the chamber 71 by the gas supply system 72 and adhered to the inner wall of the chamber 71 and the surface of the wafer W. The moisture may be evaporated, whereby the moisture contained in the gas in the chamber 71 can be removed. When the inside of the chamber 71 is evacuated by the LL / M exhaust system 73, the inside of the chamber 71 is removed. The moisture contained in the gas can be prevented from solidifying due to adiabatic expansion.

また、ガス供給系72によりチャンバ71内に、LL/M排気系73によるチャンバ71内の真空排気の際における断熱膨張によりチャンバ71内のガスの温度が水分の凝固点まで低下するのを防止すべく所定の温度以上に加熱したガスを供給してもよく、これにより、チャンバ71内のガスが断熱膨張により当該ガスの温度が水分の凝固点まで低下しないので、当該ガス中に含まれる水分は凝固することがない。さらに、上述のように所定の温度以上に加熱したガスをチャンバ71内に供給するので、チャンバ71内のガスの温度をL/M51内の水分を含む大気の温度よりも高くすることができる。これにより、ゲートバルブ7を開いた際にL/M51からチャンバ71内に流れ込む水分を含む大気をチャンバ71内の下部に流れ込ませることができ、水分を含む大気がピック74のウエハ載置面に載置されたウエハWの上方に回り込むのを防止することができる。したがって、ウエハWの上方において水分が凝固するのを防止することができる。   Further, in order to prevent the gas temperature in the chamber 71 from being lowered to the moisture freezing point due to adiabatic expansion when the gas supply system 72 evacuates the chamber 71 by the LL / M exhaust system 73. A gas heated to a predetermined temperature or higher may be supplied. As a result, the gas in the chamber 71 does not decrease to the freezing point of water due to adiabatic expansion, so that the water contained in the gas is solidified. There is nothing. Further, since the gas heated to a predetermined temperature or higher is supplied into the chamber 71 as described above, the temperature of the gas in the chamber 71 can be made higher than the temperature of the atmosphere containing moisture in the L / M 51. Thereby, when the gate valve 7 is opened, the atmosphere containing moisture flowing into the chamber 71 from the L / M 51 can be caused to flow into the lower portion of the chamber 71, and the atmosphere containing moisture enters the wafer mounting surface of the pick 74. It is possible to prevent the wafer W from going around the wafer W placed thereon. Therefore, it is possible to prevent moisture from solidifying above the wafer W.

また、本実施の形態において、図4(C)に示すように、ガス供給系72によりチャンバ71内に乾燥ガスを供給し、チャンバ71内のガスの圧力をL/M51内の水分を含む大気の圧力よりも高くしてもよく、これにより、ゲートバルブ7が開いた際にL/M51内の水分を含む大気がチャンバ71内に流れ込むのを防ぐことができ、もって、チャンバ71内に水分を含んだ大気が供給されるのを防止することができる。   Further, in the present embodiment, as shown in FIG. 4C, a dry gas is supplied into the chamber 71 by the gas supply system 72, and the pressure of the gas in the chamber 71 is changed to an atmosphere containing moisture in the L / M 51. Therefore, when the gate valve 7 is opened, the atmosphere containing moisture in the L / M 51 can be prevented from flowing into the chamber 71, so that moisture in the chamber 71 can be prevented. It is possible to prevent the supply of atmospheric air.

また、本実施の形態において、図1に示すように、ガス供給系60によりL/M51内にNガスやドライエア等の乾燥ガスを供給し、L/M51内のガスを水分を含んだ大気から当該乾燥ガスに置換する。これにより、ゲートバルブ7が開いた際にLL/M4のチャンバ71内に水分を含んだ大気が流れ込むのを防ぐことができ、もって、チャンバ71内に水分を含んだ大気が供給されるのを防止することができる。また、上記した水分を分解するガスをガス供給系60によりL/M51内に供給し、L/M51内の大気中に含まれる水分を分解することによっても、同様の効果が得られる。 Further, in the present embodiment, as shown in FIG. 1, a dry gas such as N 2 gas or dry air is supplied into the L / M 51 by the gas supply system 60, and the gas in the L / M 51 contains the moisture. To the dry gas. As a result, when the gate valve 7 is opened, it is possible to prevent the atmosphere containing moisture from flowing into the chamber 71 of the LL / M4, so that the atmosphere containing moisture can be supplied into the chamber 71. Can be prevented. Further, the same effect can be obtained by supplying the gas for decomposing the moisture into the L / M 51 by the gas supply system 60 and decomposing the moisture contained in the atmosphere in the L / M 51.

本発明の第1の実施の形態に係る基板処理システムの概略構成を示す断面図である。It is sectional drawing which shows schematic structure of the substrate processing system which concerns on the 1st Embodiment of this invention. 図1におけるLL/Mにおいて実行される真空排気処理を説明する図である。It is a figure explaining the evacuation process performed in LL / M in FIG. 図2の真空排気処理の変形例を示す図であり、(A)は排気速度を制御する場合であり、(B)は冷却装置を設ける場合であり、(C)はカーテン状流れのガスを噴出する場合である。It is a figure which shows the modification of the evacuation process of FIG. 2, (A) is a case where exhaust_gas | exhaustion speed is controlled, (B) is a case where a cooling device is provided, (C) is a gas of curtain-like flow. It is a case of erupting. 図2の真空排気処理の変形例を示す図であり、(A)は乾燥ガス等を供給する場合であり、(B)は加熱したガスを供給する場合であり、(C)はチャンバ内の圧力を高める場合である。It is a figure which shows the modification of the evacuation process of FIG. 2, (A) is a case where dry gas etc. are supplied, (B) is a case where heated gas is supplied, (C) is in a chamber. This is when the pressure is increased.

符号の説明Explanation of symbols

1 基板処理システム
2 プロセスモジュール
3 大気系搬送装置
4 ロード・ロックモジュール
51 ローダーモジュール
60,72 ガス供給系
70 移載アーム
73 LL/M排気系
74 ピック
90 板状部材
DESCRIPTION OF SYMBOLS 1 Substrate processing system 2 Process module 3 Atmospheric transfer device 4 Load lock module 51 Loader module 60, 72 Gas supply system 70 Transfer arm 73 LL / M exhaust system 74 Pick 90 Plate-like member

Claims (13)

内部が第1の圧力で水分を含む第1の環境にある第1室と内部が第1の圧力よりも低い第2の圧力の第2の環境にある第2室との間に設けられ、当該第1室と当該第2室との間で双方向に基板を搬送し且つ当該基板を支持する支持部を有する搬送装置を備えた中間搬送室において、
前記中間搬送室の内部圧力を前記第1の圧力から前記第2の圧力へ減圧すべく当該中間搬送室内を排気する排気装置と、
該排気装置による排気の際に、前記支持部に支持された基板の直上のガスのコンダクタンスを制御するコンダクタンス制御装置とを備え、
前記コンダクタンス制御装置は前記基板の主面と対向して設けられた平板状部材であり、且つ、前記平板状部材は加熱手段を備えず、前記排気装置による排気の際に前記平板状部材によって前記基板を加熱することなく前記基板の主面上において水分の凝結若しくは凝縮が生じないように、前記基板の主面と前記平板状部材との間隔を制御することによって前記基板の直上のガスのコンダクタンスを制御することを特徴とする中間搬送室。
The first chamber is provided between a first chamber in a first environment containing moisture at a first pressure and a second chamber in a second environment having a second pressure lower than the first pressure. In the intermediate transfer chamber provided with a transfer device having a support part for transferring the substrate bidirectionally between the first chamber and the second chamber and supporting the substrate,
An exhaust device for exhausting the intermediate transfer chamber to reduce the internal pressure of the intermediate transfer chamber from the first pressure to the second pressure;
A conductance control device for controlling the conductance of the gas immediately above the substrate supported by the support portion when exhausting by the exhaust device;
The conductance controller is a plate member provided in the main surface facing the substrate, and the plate-like member is not provided with a heating means, by the plate member at the time of the exhaust gas by the exhaust device By controlling the distance between the main surface of the substrate and the flat plate member so as not to cause condensation or condensation of moisture on the main surface of the substrate without heating the substrate , An intermediate transfer chamber characterized by controlling conductance.
前記排気装置は前記基板の主面上の水分の凝結若しくは凝縮が生じない最大の排気速度で当該中間搬送室内の排気を行うことを特徴とする請求項1記載の中間搬送室。 The exhaust system intermediate chamber according to claim 1 Symbol placement and performing maximum exhaust of the intermediate transfer chamber at a pumping speed condensation or condensation of moisture on the main surface of the substrate does not occur. さらに、前記中間搬送室内の水分量を測定する水分量測定装置を備え、
前記排気装置は当該水分量測定装置の測定結果に基づいて当該中間搬送室内の排気を行うことを特徴とする請求項記載の中間搬送室。
Furthermore, a water content measuring device for measuring the water content in the intermediate transfer chamber is provided,
3. The intermediate transfer chamber according to claim 2, wherein the exhaust device exhausts the intermediate transfer chamber based on a measurement result of the moisture amount measuring device.
さらに、前記中間搬送室内の凝結若しくは凝縮した水分を検出する水分検出装置を備え、
前記排気装置は当該水分検出装置の検出結果に基づいて当該中間搬送室内の排気を行うことを特徴とする請求項又は記載の中間搬送室。
Furthermore, a moisture detection device for detecting condensed or condensed moisture in the intermediate transfer chamber is provided,
The exhaust system intermediate chamber according to claim 2 or 3, wherein the performing evacuation of the intermediate transfer chamber on the basis of the detection result of the moisture detection device.
さらに、前記中間搬送室内に乾燥したガスを供給する乾燥ガス供給装置を備えることを特徴とする請求項1乃至のいずれか1項に記載の中間搬送室。 The intermediate transfer chamber according to any one of claims 1 to 4 , further comprising a dry gas supply device for supplying a dry gas into the intermediate transfer chamber. さらに、前記中間搬送室内に所定の温度に加熱したガスを供給する加熱ガス供給装置を備えることを特徴とする請求項1乃至のいずれか1項に記載の中間搬送室。 Further, an intermediate transfer chamber according to any one of claims 1 to 5, characterized in that it comprises a heating gas supply apparatus for supplying the heated on the intermediate transfer chamber to a predetermined temperature gas. さらに、前記中間搬送室内に該中間搬送室内を前記第1の圧力よりも高い圧力に昇圧するガスを供給する昇圧ガス供給装置を備えることを特徴とする請求項1乃至のいずれか1項に記載の中間搬送室。 The pressure rising gas supply device according to any one of claims 1 to 6 , further comprising a gas supply device for supplying a gas for increasing the pressure in the intermediate transfer chamber to a pressure higher than the first pressure. The intermediate transfer chamber described. さらに、前記中間搬送室内に該中間搬送室内に含まれる水分を分解するガスを供給する水分分解ガス供給装置を備えることを特徴とする請求項1乃至のいずれか1項に記載の中間搬送室。 The intermediate transfer chamber according to any one of claims 1 to 7 , further comprising a moisture decomposition gas supply device that supplies a gas for decomposing moisture contained in the intermediate transfer chamber into the intermediate transfer chamber. . さらに、前記中間搬送室における前記第1室との連通部において当該第1室内のガスの当該中間搬送室内への侵入を遮断するガスを噴出する遮断ガス噴出手段を備えることを特徴とする請求項1乃至のいずれか1項に記載の中間搬送室。 Furthermore, the said intermediate conveyance chamber is provided with the interruption | blocking gas injection means which injects the gas which interrupts | blocks the penetration | invasion into the said intermediate conveyance chamber in the communication part with the said 1st chamber in the said intermediate conveyance chamber. The intermediate transfer chamber according to any one of 1 to 8 . さらに、前記中間搬送室内及び内壁の少なくとも一部を冷却する冷却手段を備えることを特徴とする請求項1乃至のいずれか1項に記載の中間搬送室。 Further, an intermediate transfer chamber according to any one of claims 1 to 9, characterized in that it comprises a cooling means for cooling at least a portion of the intermediate transfer chamber and the inner wall. 前記第1室内には乾燥したガスが供給されることを特徴とする請求項1乃至10のいずれか1項に記載の中間搬送室。 The intermediate transfer chamber according to any one of claims 1 to 10 , wherein a dry gas is supplied into the first chamber. 前記第2室としての基板に処理を施す基板処理装置と、前記第1室としての前記基板を搬送する基板搬送装置と、請求項1乃至11のいずれか1項に記載の中間搬送室とを備えることを特徴とする基板処理システム。 A substrate processing apparatus for processing a substrate as the second chamber, a substrate transfer apparatus for transferring the substrate as the first chamber, and the intermediate transfer chamber according to any one of claims 1 to 11. A substrate processing system comprising: 内部が第1の圧力で水分を含む第1の環境にある第1室と内部が第1の圧力よりも低い第2の圧力の第2の環境にある第2室との間に設けられ、当該第1室と当該第2室との間で双方向に基板を搬送し且つ当該基板を支持する支持部を有する搬送装置を備えた中間搬送室の排気方法において、
前記中間搬送室の内部圧力を前記第1の圧力から前記第2の圧力へ減圧すべく当該中間搬送室内を排気する排気ステップと、
該排気ステップによる排気の際に、前記支持部に支持された基板の直上のガスのコンダクタンスを制御するコンダクタンス制御ステップとを有し、
前記コンダクタンス制御ステップでは、加熱手段を備えない平板状部材を前記基板の主面と対向するように配置し、前記平板状部材によって前記基板を加熱することなく、前記基板の主面上において水分の凝結若しくは凝縮が生じないように、前記基板の主面と前記平板状部材との間隔を制御することによって前記基板の直上のガスのコンダクタンスを制御することを特徴とする中間搬送室の排気方法。
The first chamber is provided between a first chamber in a first environment containing moisture at a first pressure and a second chamber in a second environment having a second pressure lower than the first pressure. In the exhaust method of the intermediate transfer chamber provided with a transfer device having a support part for transferring the substrate bidirectionally between the first chamber and the second chamber and supporting the substrate,
An exhaust step of exhausting the intermediate transfer chamber to reduce the internal pressure of the intermediate transfer chamber from the first pressure to the second pressure;
A conductance control step for controlling the conductance of the gas immediately above the substrate supported by the support portion during exhaust by the exhaust step;
In the conductance control step, a flat plate-like member not provided with a heating means is disposed so as to face the main surface of the substrate, and moisture is not formed on the main surface of the substrate without heating the substrate by the flat plate-like member. An exhaust method for an intermediate transfer chamber, wherein the conductance of gas immediately above the substrate is controlled by controlling the distance between the main surface of the substrate and the flat plate member so that condensation or condensation does not occur.
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Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5090291B2 (en) * 2008-08-18 2012-12-05 大日本スクリーン製造株式会社 Substrate processing equipment
JP5295808B2 (en) 2009-02-09 2013-09-18 東京エレクトロン株式会社 Particle adhesion prevention method and substrate transport method
JP2010219228A (en) * 2009-03-16 2010-09-30 Hitachi Kokusai Electric Inc Substrate processing apparatus
JP2011077096A (en) * 2009-09-29 2011-04-14 Hitachi High-Tech Instruments Co Ltd Electronic component mounting apparatus, component feeder, and method of mounting electronic component
KR101130558B1 (en) * 2009-10-27 2012-03-30 주식회사 테스 Transfer Chamber having Plate for Heat Exchange and Semiconductor Fabrication Equipment having The same
CN104210844B (en) * 2014-09-10 2016-11-02 深圳市华星光电技术有限公司 Glass substrate transmission system and mechanical hand thereof
CN106531658B (en) * 2015-09-10 2020-03-31 北京北方华创微电子装备有限公司 Pressure control method and device
JP7458267B2 (en) 2020-08-19 2024-03-29 東京エレクトロン株式会社 SUBSTRATE PROCESSING APPARATUS AND SUBSTRATE TRANSFER METHOD
TWI763518B (en) * 2021-06-02 2022-05-01 南亞科技股份有限公司 Wafer container

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2970889B2 (en) * 1991-06-05 1999-11-02 東京エレクトロン株式会社 Exhaust port structure of vacuum vessel
JP2818054B2 (en) * 1991-06-22 1998-10-30 克嘉 蓼沼 Water decomposing agent, method for decomposing and decomposing water on material surface using the same, method for decomposing and removing water in gas, and their devices
US5308989A (en) * 1992-12-22 1994-05-03 Eaton Corporation Fluid flow control method and apparatus for an ion implanter
JPH06196540A (en) * 1992-12-25 1994-07-15 Hitachi Ltd Vacuum device
JP3394293B2 (en) * 1993-09-20 2003-04-07 株式会社日立製作所 Method for transporting sample and method for manufacturing semiconductor device
JP3471077B2 (en) * 1993-12-24 2003-11-25 東京エレクトロン株式会社 Vacuum vessel pressure control method
JPH08124993A (en) * 1994-10-27 1996-05-17 Kokusai Electric Co Ltd Load locking chamber for semiconductor production device
JPH09129709A (en) * 1995-10-27 1997-05-16 Nec Corp Processing apparatus
JPH10144581A (en) * 1996-11-14 1998-05-29 Kokusai Electric Co Ltd Semiconductor device
JPH10173025A (en) * 1996-12-16 1998-06-26 Kokusai Electric Co Ltd Load lock chamber of semiconductor manufacturing device
JP2000195925A (en) * 1998-12-28 2000-07-14 Anelva Corp Substrate-treating device
JP3595756B2 (en) * 2000-06-01 2004-12-02 キヤノン株式会社 Exposure apparatus, lithography apparatus, load lock apparatus, device manufacturing method, and lithography method
US6808566B2 (en) * 2001-09-19 2004-10-26 Tokyo Electron Limited Reduced-pressure drying unit and coating film forming method
JP2007049046A (en) * 2005-08-11 2007-02-22 Hitachi Kokusai Electric Inc Semiconductor device manufacturing method

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