JP2009038210A - Vapor dryer - Google Patents

Vapor dryer Download PDF

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JP2009038210A
JP2009038210A JP2007201039A JP2007201039A JP2009038210A JP 2009038210 A JP2009038210 A JP 2009038210A JP 2007201039 A JP2007201039 A JP 2007201039A JP 2007201039 A JP2007201039 A JP 2007201039A JP 2009038210 A JP2009038210 A JP 2009038210A
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vapor
substrate
quartz glass
ipa
supply pipe
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JP4705937B2 (en
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Hajime Onoda
元 小野田
Kazutoshi Watanabe
和俊 渡辺
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OMEGA SEMICON DENSHI KK
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OMEGA SEMICON DENSHI KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a vapor dryer which not only forms vapor instantaneously with supplying the vapor on a substrate for drying, but also performs clean cleaning and clean drying without causing any corrosion. <P>SOLUTION: A vapor dryer comprises a cleaning device which supports a substrate W, a process liquid feeding unit 31 which selectively supplies two or more kinds of process liquid, a quartz glass tube 14 having one end connected to the process liquid feeding unit 31 and the other end having a vapor supply pipe 26 connected to the cleaning device and having a channel to circulate the process liquid supplied from the process liquid feeding unit 31, a rod heater 27 installed inside the quartz glass tube 14 separately from the channel, and a halogen lamp 28 installed outside the quartz glass tube 14 to heat the rod heater 27, serving as a heating means to heat or vaporize the process liquid circulating in the channel by radiant heat and supplying it to the vapor supply pipe 26. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、半導体基板、液晶基板等を洗浄した後、乾燥するベーパー乾燥装置に関する。   The present invention relates to a vapor drying apparatus that cleans a semiconductor substrate, a liquid crystal substrate, and the like and then dries.

半導体基板、液晶基板等を洗浄する洗浄装置として、本出願人は、水素と酸素を容器内で燃焼させ、酸素とオゾンとラジカル酸素を含んだ水蒸気を生成し、この生成した水蒸気を水蒸気供給ノズルによって前記基板の表面に噴射して洗浄する洗浄装置を開発し、特許文献1として特許を取得している。   As a cleaning device for cleaning a semiconductor substrate, a liquid crystal substrate, etc., the present applicant generates hydrogen vapor containing oxygen, ozone, and radical oxygen by burning hydrogen and oxygen in a container, and uses the generated water vapor as a water vapor supply nozzle. Has developed a cleaning apparatus that sprays and cleans the surface of the substrate, and has obtained a patent as Patent Document 1.

この洗浄装置は、燃焼後の水蒸気を水蒸気供給ノズルによって基板の表面に噴射して洗浄するため、オゾン発生から基板までの配管が長くても、自己分解することなく高濃度のオゾンを基板に供給でき、基板を任意の位置に設置できるという効果がある。   This cleaning device injects the water vapor after combustion onto the surface of the substrate by the water vapor supply nozzle, so that even if the piping from the generation of ozone to the substrate is long, high concentration ozone is supplied to the substrate without self-decomposition. This is advantageous in that the substrate can be installed at an arbitrary position.

さらに、基板の表面に水蒸気を噴射した後、所定時間だけ基板上に有機溶剤としてイソプロピルアルコール(isopropyl alcohol :以下IPAと呼ぶ)を供給するIPA蒸気供給管を設けている。IPA蒸気供給管は、基端側がIPA供給口及び純水供給口に接続され、先端側は前記水蒸気供給ノズルに対向している。そして、水蒸気供給管の内部を流れる数百℃のオゾン水蒸気HO+OによってIPA蒸気供給管を加温し、IPA蒸気供給管内でIPA蒸気が凝縮することなく、水蒸気供給ノズルから噴射することができる。 Further, an IPA vapor supply pipe for supplying isopropyl alcohol (hereinafter referred to as IPA) as an organic solvent on the substrate for a predetermined time after water vapor is sprayed on the surface of the substrate is provided. The IPA vapor supply pipe has a proximal end connected to the IPA supply port and the pure water supply port, and a distal end facing the water vapor supply nozzle. Then, the IPA vapor supply pipe is heated by ozone water vapor H 2 O + O 3 of several hundred degrees Celsius flowing inside the water vapor supply pipe, and the IPA vapor is injected from the water vapor supply nozzle without condensing in the IPA vapor supply pipe. it can.

また、従来、IPAベーパー発生装置は市販されている。このIPAベーパー発生装置はステンレス製の加熱エレメント管であり、この加熱エレメント管の外周にワークコイルが設けられ、ワークコイルに高周波電流が流れると、磁束が発生して加熱エレメント管に誘導電流が流れてIPAガスが加熱されるように構成されている。   Conventionally, IPA vapor generators are commercially available. This IPA vapor generator is a heating element tube made of stainless steel. A work coil is provided on the outer periphery of the heating element tube. When a high frequency current flows through the work coil, a magnetic flux is generated and an induced current flows through the heating element tube. Thus, the IPA gas is heated.

また、半導体基板をドライ酸化処理するクリーンガス加熱装置として、特許文献2が知られている。このクリーンガス加熱装置は、一端側がガス供給側に、他端側がガス需要側に接続された石英ガラス管の内部にガス供給側から供給されたクリーンガスを加熱するSiCからなるガス加熱管が設けられている。そして、石英ガラス管の外部からガス加熱管を加熱するハロゲンランプを設け、常温のクリーンガスがSiCからなるガス加熱管の内部を通過する際に、高温度に加熱され、ガス需要側の半導体基板に導かれ、半導体基板の表面に酸化膜が形成されるようになっている。
特許第3910190号公報 特許第3253176号公報
Further, Patent Document 2 is known as a clean gas heating apparatus that performs dry oxidation treatment on a semiconductor substrate. This clean gas heating device is provided with a gas heating tube made of SiC that heats clean gas supplied from the gas supply side inside a quartz glass tube with one end connected to the gas supply side and the other end connected to the gas demand side. It has been. Then, a halogen lamp that heats the gas heating tube from the outside of the quartz glass tube is provided, and when the clean gas at normal temperature passes through the inside of the gas heating tube made of SiC, it is heated to a high temperature, and the semiconductor substrate on the gas demand side Thus, an oxide film is formed on the surface of the semiconductor substrate.
Japanese Patent No. 3910190 Japanese Patent No. 3253176

前述した特許文献1のものは、水蒸気供給管の内部を流れる数百℃のオゾン水蒸気HO+OによってIPA蒸気供給管を加温することができるが、液体のIPAを瞬時にベーパーとして供給することは困難であり、基板を乾燥する装置としては不向きである。 In the above-mentioned Patent Document 1, the IPA vapor supply pipe can be heated by ozone water vapor H 2 O + O 3 of several hundred degrees Celsius flowing inside the water vapor supply pipe, but liquid IPA is instantaneously supplied as vapor. This is difficult and is not suitable as an apparatus for drying a substrate.

また、市販のIPAベーパー発生装置は、ステンレス製の加熱エレメント管を採用しているため、IPAベーパーが加熱されたステンレスと接して汚染されるという問題がある。   In addition, since a commercially available IPA vapor generator employs a heating element tube made of stainless steel, there is a problem that the IPA vapor is contaminated in contact with the heated stainless steel.

本発明は、前記事情に着目してなされたもので、その目的とするところは、瞬時にベーパーを生成して基板上に供給して基板を乾燥でき、しかも腐食されることなく、クリーンな洗浄及び乾燥ができるベーパー乾燥装置を提供することにある。   The present invention has been made paying attention to the above-mentioned circumstances, and its purpose is to generate a vapor instantly and supply it onto the substrate to dry the substrate, and clean cleaning without being corroded. And providing a vapor drying apparatus capable of drying.

本発明は、前記目的を達成するために、請求項1は、基板を支持する洗浄装置と、複数種類の処理液を選択的に供給する処理液供給ユニットと、一端側が前記処理液供給ユニットに接続され、他端側に前記洗浄装置に接続されるベーパー供給管を有し、前記処理液供給ユニットから供給された処理液を流通する流通路を有する石英ガラス管と、前記石英ガラス管の内側に前記流通路と隔離された状態に設けられたロッドヒーターと、前記石英ガラス管の外側に設けられ、前記ロッドヒーターを加熱し、輻射熱によって前記流通路を流通する前記処理液を加熱あるいは気化して前記ベーパー供給管に導く加熱手段とを具備したことを特徴とするベーパー乾燥装置にある。   In order to achieve the above object, the present invention provides a cleaning apparatus that supports a substrate, a treatment liquid supply unit that selectively supplies a plurality of types of treatment liquids, and one end side of the treatment liquid supply unit. A quartz glass tube having a vapor supply pipe connected to the other end side and connected to the cleaning device, and having a flow path for flowing the processing liquid supplied from the processing liquid supply unit; and an inner side of the quartz glass pipe A rod heater provided in a state isolated from the flow passage, and provided outside the quartz glass tube, heats the rod heater and heats or vaporizes the treatment liquid flowing through the flow passage by radiant heat. And a heating means that leads to the vapor supply pipe.

請求項2は、請求項1の前記洗浄装置は、枚葉洗浄装置またはワンバス洗浄装置であり、基板に対して純水を噴射する純水噴射手段を備えていることを特徴とする。   According to a second aspect of the present invention, the cleaning apparatus according to the first aspect is a single wafer cleaning apparatus or a one-bus cleaning apparatus, and includes a pure water injection unit that injects pure water onto the substrate.

請求項3は、請求項1の前記処理液供給ユニットは、洗浄薬液、IPA液、窒素を選択的に供給する複数の供給弁及び前記石英ガラス管に定量供給する定量供給手段を備えていることを特徴とする。   According to a third aspect of the present invention, the processing liquid supply unit according to the first aspect includes a plurality of supply valves for selectively supplying cleaning chemical liquid, IPA liquid, and nitrogen, and a quantitative supply means for supplying a fixed quantity to the quartz glass tube. It is characterized by.

本発明によれば、瞬時にベーパーを生成して基板上に供給して基板を乾燥できる。また、処理液が接触する部分は全て石英ガラスであり、腐食されることはなく、クリーンな洗浄及び乾燥ができるという効果がある。   According to the present invention, vapor can be instantaneously generated and supplied onto the substrate to dry the substrate. Further, all the parts that come into contact with the treatment liquid are quartz glass, and there is an effect that the parts are not corroded and can be cleaned and dried.

以下、本発明の実施の形態を図面に基づいて説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は第1の実施形態のベーパー乾燥装置の全体構成を示し、有機溶剤としてのIPAベーパー生成装置11を備えている。まず、IPAベーパー生成装置11について説明すると、装置本体12には横方向に円筒状の空洞部13が設けられている。空洞部13には円筒状の高純度の石英ガラス管14が設けられている。石英ガラス管14は外筒15と内筒16からなる二重管構造で、外筒15と内筒16との間には環状空間部が形成され、この環状空間部には高純度の石英ガラス製の仕切り管17が介在されている。そして、仕切り管17の外側には外側流通路18が設けられ、内側には内側流通路19が設けられている。さらに、仕切り管17の一端部には外側流通路18と内側流通路19とを連通する折り返し部20が設けられている。そして、処理液が外側流通路18から折り返し部20を介して内側流通路19へ流れるようになっている。   FIG. 1 shows the overall configuration of the vapor drying apparatus according to the first embodiment, which includes an IPA vapor generating apparatus 11 as an organic solvent. First, the IPA vapor generating apparatus 11 will be described. The apparatus main body 12 is provided with a cylindrical hollow portion 13 in the lateral direction. The hollow portion 13 is provided with a cylindrical high-purity quartz glass tube 14. The quartz glass tube 14 has a double tube structure composed of an outer cylinder 15 and an inner cylinder 16, and an annular space is formed between the outer cylinder 15 and the inner cylinder 16, and high purity quartz glass is formed in the annular space. The partition pipe 17 made from is interposed. An outer flow passage 18 is provided outside the partition tube 17, and an inner flow passage 19 is provided inside. Furthermore, a folded portion 20 that connects the outer flow passage 18 and the inner flow passage 19 is provided at one end of the partition pipe 17. Then, the processing liquid flows from the outer flow passage 18 to the inner flow passage 19 through the folded portion 20.

外筒15の軸方向の一端部は入口側端板21によって封止され、他端部は出口側端板22によって封止されており、入口側端板21には窒素供給管23と処理液供給管24が設けられている。また、内筒16の更に内側には高純度の石英ガラス製の中央流通管25が設けられ、中央流通管25の一端部は内側流通路19と連通し、他端部はベーパー供給管26に連通している。   One end of the outer cylinder 15 in the axial direction is sealed by an inlet side end plate 21, and the other end is sealed by an outlet side end plate 22. The inlet side end plate 21 has a nitrogen supply pipe 23 and a processing solution. A supply pipe 24 is provided. Further, a central flow pipe 25 made of high-purity quartz glass is provided further inside the inner cylinder 16. One end of the central flow pipe 25 communicates with the inner flow passage 19, and the other end is connected to the vapor supply pipe 26. Communicate.

内筒16と中央流通管25との間は密閉された環状空間に形成され、環状空間には例えばSiCあるいはカーボン等からなるロッドヒーター27が密閉された状態に設けられている。また、装置本体12の内部には加熱手段として複数本の直管形のハロゲンランプ28が設けられ、これらハロゲンランプ28は石英ガラス管14を囲繞するように周方向に等間隔に配置されている。ロッドヒーター27に向かって赤外線を照射するようになっており、ロッドヒーター27には温度センサ29が設けられている。温度センサ29の検出信号は装置本体12の外部に設けられた加熱制御ユニット30に入力され、ハロゲンランプ28の出力を制御するようになっている。ロッドヒーター27の温度を、例えば常時200℃に保つように加熱制御ユニット30が制御するようになっている。   A space between the inner cylinder 16 and the central flow pipe 25 is formed in a sealed annular space, and a rod heater 27 made of, for example, SiC or carbon is provided in the annular space in a sealed state. In addition, a plurality of straight tube halogen lamps 28 are provided inside the apparatus body 12 as heating means, and these halogen lamps 28 are arranged at equal intervals in the circumferential direction so as to surround the quartz glass tube 14. . The rod heater 27 is irradiated with infrared rays, and the rod heater 27 is provided with a temperature sensor 29. A detection signal of the temperature sensor 29 is input to a heating control unit 30 provided outside the apparatus main body 12 so as to control the output of the halogen lamp 28. The heating control unit 30 is controlled so that the temperature of the rod heater 27 is always kept at 200 ° C., for example.

一方、装置本体11の外部には処理液供給ユニット31が設けられている。処理液供給ユニット31には薬液供給源32が設けられ、薬液供給源32はマスフローコントローラ32aを介して薬液供給弁32bに接続されている。処理液供給ユニット31にはIPA貯溜タンク33が設けられ、このIPA貯溜タンク33の供給口はIPA供給定量ポンプ33aを介してIPA供給弁33bに接続されている。さらに、処理液供給ユニット31には窒素供給源34が設けられ、窒素供給源34はマスフローコントローラ34aを介して第1の窒素供給弁34b及び第2の窒素供給弁34cに接続されている。   On the other hand, a processing liquid supply unit 31 is provided outside the apparatus main body 11. The treatment liquid supply unit 31 is provided with a chemical liquid supply source 32, and the chemical liquid supply source 32 is connected to a chemical liquid supply valve 32b via a mass flow controller 32a. The treatment liquid supply unit 31 is provided with an IPA storage tank 33, and the supply port of the IPA storage tank 33 is connected to an IPA supply valve 33b via an IPA supply metering pump 33a. Further, the treatment liquid supply unit 31 is provided with a nitrogen supply source 34, and the nitrogen supply source 34 is connected to the first nitrogen supply valve 34b and the second nitrogen supply valve 34c via the mass flow controller 34a.

そして、第1の窒素供給弁34bは第1の配管35aを介して窒素供給管23に接続され、薬液供給弁32b、IPA供給弁33b及び第2の窒素供給弁34cは第2の配管35bを介して処理液供給管24に接続されている。   The first nitrogen supply valve 34b is connected to the nitrogen supply pipe 23 via the first pipe 35a, and the chemical liquid supply valve 32b, the IPA supply valve 33b, and the second nitrogen supply valve 34c are connected to the second pipe 35b. To the processing liquid supply pipe 24.

また、前記ベーパー供給管26は枚葉洗浄装置のチャンバ36に接続されている。枚葉洗浄装置にはチャンバ36に対向し、回転軸37を中心として回転する基板載置台38が設けられ、この基板載置台38には洗浄・乾燥すべき半導体基板、液晶基板等の基板Wが載置されている。さらに、ベーパー供給管26には純水供給管39が内挿され、基板Wの上面の中央部には純水供給管39の出口に設けられた純水供給ノズル40が対向して設けられている。基板Wと純水供給ノズル40の距離Hは数mmに設定され、基板Wの周囲には排気口41が設けられている。純水供給管39の基端側は純水供給源42に接続されている。   The vapor supply pipe 26 is connected to a chamber 36 of the single wafer cleaning apparatus. The single wafer cleaning apparatus is provided with a substrate mounting table 38 that is opposed to the chamber 36 and rotates about a rotation shaft 37. The substrate mounting table 38 includes a substrate W such as a semiconductor substrate or a liquid crystal substrate to be cleaned and dried. It is placed. Further, a pure water supply pipe 39 is inserted in the vapor supply pipe 26, and a pure water supply nozzle 40 provided at the outlet of the pure water supply pipe 39 is provided opposite to the central portion of the upper surface of the substrate W. Yes. A distance H between the substrate W and the pure water supply nozzle 40 is set to several mm, and an exhaust port 41 is provided around the substrate W. The base end side of the pure water supply pipe 39 is connected to a pure water supply source 42.

次に、前述のように構成されたベーパー乾燥装置を用いてチャンバ36の内部の基板載置台38に載置された基板Wを洗浄・乾燥する方法について説明する。   Next, a method for cleaning and drying the substrate W mounted on the substrate mounting table 38 inside the chamber 36 using the vapor drying apparatus configured as described above will be described.

図2に示すように、基板載置台38に洗浄・乾燥すべき基板Wを載置する。次に、IPAベーパー生成装置11を回転しながら水平方向に移動させるとともに下降させると、図3に示すように、基板Wが載置された基板載置台38にチャンバ36が対向する。同時に、純水供給管39の純水供給ノズル40が基板Wの中央部に対向する。   As shown in FIG. 2, the substrate W to be cleaned and dried is placed on the substrate platform 38. Next, when the IPA vapor generating apparatus 11 is rotated and moved in the horizontal direction, the chamber 36 faces the substrate mounting table 38 on which the substrate W is mounted, as shown in FIG. At the same time, the pure water supply nozzle 40 of the pure water supply pipe 39 faces the central portion of the substrate W.

次に、図4に示すように、純水供給源42から純水供給管39に対して純水を供給すると、純水供給ノズル40を介して基板Wの上面に純水が供給される。このとき、基板載置台38は回転軸37を中心として回転させるため、基板Wは枚葉スピン洗浄され、基板W上の水滴は遠心力によって周囲に飛散される。   Next, as shown in FIG. 4, when pure water is supplied from the pure water supply source 42 to the pure water supply pipe 39, pure water is supplied to the upper surface of the substrate W through the pure water supply nozzle 40. At this time, since the substrate mounting table 38 is rotated about the rotation shaft 37, the substrate W is subjected to single wafer spin cleaning, and water droplets on the substrate W are scattered around by centrifugal force.

基板Wを洗浄した後、IPAベーパー生成装置11から水洗後の基板Wに対して薬液を供給したり、IPAベーパーを供給して基板W上の水滴と薬液または水滴とIPAとを置換することができるが、本実施形態においては、薬液を供給したのち、IPAベーパーを供給する場合について説明する。   After cleaning the substrate W, the chemical solution may be supplied from the IPA vapor generating device 11 to the substrate W after being washed, or the IPA vapor may be supplied to replace the water droplet and the chemical solution or the water droplet and the IPA on the substrate W. However, in the present embodiment, a case where IPA vapor is supplied after supplying a chemical solution will be described.

まず、処理液供給ユニット31の薬液供給弁32bを開弁すると、薬液供給源32から薬液が供給され、この薬液は第2の配管35b及び処理液供給管24を介してIPAベーパー生成装置11に供給される。このとき、装置本体12内のハロゲンランプ28の出力は加熱制御ユニット30によって制御されており、ハロゲンランプ28からの赤外線はロッドヒーター27に向かって照射される。ロッドヒーター27はハロゲンランプ28によって200℃に加熱される。   First, when the chemical liquid supply valve 32b of the processing liquid supply unit 31 is opened, the chemical liquid is supplied from the chemical liquid supply source 32, and this chemical liquid is supplied to the IPA vapor generator 11 via the second pipe 35b and the processing liquid supply pipe 24. Supplied. At this time, the output of the halogen lamp 28 in the apparatus main body 12 is controlled by the heating control unit 30, and infrared rays from the halogen lamp 28 are irradiated toward the rod heater 27. The rod heater 27 is heated to 200 ° C. by a halogen lamp 28.

従って、常温の薬液は、IPAベーパー生成装置11の外側流通路18を流れてガス折り返し部20で折り返して内側流通路19に流れ、さらに中央流通管25の内部を流れてベーパー供給管26に至る。このとき、ロッドヒーター27は、石英ガラスによって密閉された状態にあり、薬液とは完全に非接触状態にあるため、薬液によって腐食されることはなく、パーティクルの発生がない。しかも、常温の薬液はロッドヒーター27によって加熱された石英ガラス管14及びが中央流通管25に接触するため、瞬時に加熱されて加熱薬液となり、ベーパー供給管26を介して基板Wに噴射される。   Therefore, the chemical solution at room temperature flows through the outer flow passage 18 of the IPA vapor generating device 11, is turned back by the gas turn-back portion 20, flows to the inner flow passage 19, and further flows through the central flow pipe 25 to the vapor supply pipe 26. . At this time, the rod heater 27 is in a state of being sealed with quartz glass and is in a completely non-contact state with the chemical liquid, so that it is not corroded by the chemical liquid and no particles are generated. In addition, since the quartz glass tube 14 heated by the rod heater 27 and the central flow tube 25 are in contact with the chemical solution at room temperature, the chemical solution is instantaneously heated to become a heated chemical solution and sprayed onto the substrate W through the vapor supply tube 26. .

このとき、図5に示すように、基板載置台38に載置された水洗後の基板Wには水滴が残っているが、加熱薬液が基板Wに供給されると、基板W上の水滴と薬液とが置換される。次に、薬液供給弁32bを閉弁し、第1の窒素供給弁34bを開弁すると、窒素供給源34から窒素が第1の配管35aを介して窒素供給管23に供給される。   At this time, as shown in FIG. 5, water droplets remain on the washed substrate W placed on the substrate platform 38, but when the heated chemical solution is supplied to the substrate W, The chemical solution is replaced. Next, when the chemical liquid supply valve 32b is closed and the first nitrogen supply valve 34b is opened, nitrogen is supplied from the nitrogen supply source 34 to the nitrogen supply pipe 23 via the first pipe 35a.

従って、常温の窒素は、IPAベーパー生成装置11の外側流通路18を流れてガス折り返し部20で折り返して内側流通路19に流れ、さらに中央流通管25の内部を流れてベーパー供給管26に至る。このとき、ロッドヒーター27は、石英ガラスによって密閉された状態にあり、窒素とは完全に非接触状態にあり、加熱された窒素がベーパー供給管26を介して基板Wに噴射される。   Therefore, nitrogen at normal temperature flows through the outer flow passage 18 of the IPA vapor generator 11, is turned back by the gas turn-back portion 20, flows to the inner flow passage 19, and further flows through the central flow pipe 25 to the vapor supply pipe 26. . At this time, the rod heater 27 is in a state of being sealed with quartz glass, and is completely in a non-contact state with nitrogen, and the heated nitrogen is sprayed onto the substrate W through the vapor supply pipe 26.

次に、第1の窒素供給弁34bを閉弁し、IPA供給弁33bを開弁すると、IPA貯溜タンク33からIPAが供給され、IPAはIPA供給定量ポンプ33aによって1〜10cc/minに設定され、第2の配管35bを介して処理液供給管24に供給される。窒素供給源34から窒素が第1の配管35aを介して窒素供給管23に供給される。従って、液体のIPAは、IPAベーパー生成装置11の外側流通路18を流れてガス折り返し部20で折り返して内側流通路19に流れ、さらに中央流通管25の内部を流れてベーパー供給管26に至る間にIPAベーパーとなる。   Next, when the first nitrogen supply valve 34b is closed and the IPA supply valve 33b is opened, IPA is supplied from the IPA storage tank 33, and IPA is set to 1 to 10 cc / min by the IPA supply metering pump 33a. Then, it is supplied to the processing liquid supply pipe 24 via the second pipe 35b. Nitrogen is supplied from the nitrogen supply source 34 to the nitrogen supply pipe 23 via the first pipe 35a. Accordingly, the liquid IPA flows through the outer flow passage 18 of the IPA vapor generating device 11, is turned back by the gas turn-back portion 20, flows to the inner flow passage 19, and further flows through the central flow pipe 25 to the vapor supply pipe 26. It becomes IPA vapor in between.

このとき、ロッドヒーター27は、石英ガラスによって密閉された状態にあり、IPAとは完全に非接触状態にあり、図6に示すように、IPAベーパーがベーパー供給管26を介して基板Wに噴射される。IPAベーパーが基板Wに供給されると、基板W上の窒素とIPAベーパーとが置換される。次に、IPA供給弁33bを閉弁し、第2の窒素供給弁34cを開弁すると、窒素供給源34から窒素が第2の配管35bを介して窒素供給管23に供給される。従って、窒素は、IPAベーパー生成装置11に供給され、前述と同様に、加熱された窒素がベーパー供給管26を介して基板Wに噴射されるため、図7に示すように、基板W上のIPAは加熱窒素によって発散され、基板Wの洗浄・乾燥が完了する。   At this time, the rod heater 27 is in a state of being sealed with quartz glass and completely in a non-contact state with the IPA, and the IPA vapor is sprayed onto the substrate W through the vapor supply pipe 26 as shown in FIG. Is done. When the IPA vapor is supplied to the substrate W, the nitrogen on the substrate W and the IPA vapor are replaced. Next, when the IPA supply valve 33b is closed and the second nitrogen supply valve 34c is opened, nitrogen is supplied from the nitrogen supply source 34 to the nitrogen supply pipe 23 via the second pipe 35b. Accordingly, nitrogen is supplied to the IPA vapor generator 11 and, as described above, the heated nitrogen is sprayed onto the substrate W through the vapor supply pipe 26. Therefore, as shown in FIG. The IPA is emitted by the heated nitrogen, and the cleaning and drying of the substrate W is completed.

本実施形態によれば、IPAベーパー生成装置11によって瞬時にIPAベーパーを生成して基板W上に供給して基板W上の水滴をIPAに置換させて乾燥できる。しかも、SiCのロッドヒーター27は高純度石英ガラスで覆われ、IPAベーパーが接触する部分は全て高純度石英ガラスであり、パーティクルの発生がないという効果がある。   According to the present embodiment, IPA vapor can be instantaneously generated by the IPA vapor generator 11 and supplied onto the substrate W, and water droplets on the substrate W can be replaced with IPA and dried. In addition, the SiC rod heater 27 is covered with high-purity quartz glass, and all the portions in contact with the IPA vapor are high-purity quartz glass, and there is an effect that no particles are generated.

図8は第2の実施形態を示し、第1の実施形態と同一構成部分は同一番号を付して説明を省略する。本実施形態は、IPAベーパー生成装置11とワンバス乾燥装置45とを組み合わせたIPAベーパー乾燥装置を示す。ワンバス乾燥装置45について説明すると、基台46の上部には上部開口の洗浄槽47が設けられ、この洗浄槽47の底部には排液弁48を有する排液管49が設けられている。   FIG. 8 shows a second embodiment, and the same components as those in the first embodiment are denoted by the same reference numerals and description thereof is omitted. This embodiment shows an IPA vapor drying apparatus in which an IPA vapor generating apparatus 11 and a one-bus drying apparatus 45 are combined. The one-bath drying device 45 will be described. A cleaning tank 47 having an upper opening is provided at the upper portion of the base 46, and a drain pipe 49 having a drain valve 48 is provided at the bottom of the cleaning tank 47.

洗浄槽47の内部には複数枚の基板Wを立位状態で、しかも間隔を存して支持する基板支持台50が設けられ、この基板支持台50の両側部には純水供給ノズル51が設けられている。洗浄槽47の外周囲には純水オーバフロー槽52が設けられ、洗浄槽47をオーバフローした純水が収容されるようになっている。純水オーバフロー槽52の上部開口は蓋体53によって閉塞され、蓋体53には複数の噴射ノズル54を有するノズルヘッド55が設けられている。このノズルヘッド55にはIPAベーパー生成装置11のベーパー供給管26が接続され、噴射ノズル54から基板Wに向かってIPAベーパー及び加熱窒素を噴射できるようになっている。   A substrate support base 50 is provided inside the cleaning tank 47 to support a plurality of substrates W in an upright state with a space therebetween, and pure water supply nozzles 51 are provided on both sides of the substrate support base 50. Is provided. A pure water overflow tank 52 is provided on the outer periphery of the cleaning tank 47 so that pure water overflowing the cleaning tank 47 is accommodated therein. The upper opening of the pure water overflow tank 52 is closed by a lid 53, and the lid 53 is provided with a nozzle head 55 having a plurality of injection nozzles 54. A vapor supply pipe 26 of the IPA vapor generator 11 is connected to the nozzle head 55 so that IPA vapor and heated nitrogen can be sprayed from the spray nozzle 54 toward the substrate W.

次に、本実施形態の作用について説明する。図9(a)に示すように、待機状態においては、純水供給ノズル51から純水を供給し続けると、洗浄槽47は純水によって満たされ、オーバフローした純水は、純水オーバフロー槽52に収容される。このとき、IPAベーパー生成装置11のベーパー供給管26から窒素を供給すると、窒素は噴射ノズル54から洗浄槽47の水面に向かって噴射される。   Next, the operation of this embodiment will be described. As shown in FIG. 9A, in the standby state, if pure water is continuously supplied from the pure water supply nozzle 51, the cleaning tank 47 is filled with pure water, and the overflowed pure water is stored in the pure water overflow tank 52. Is housed. At this time, when nitrogen is supplied from the vapor supply pipe 26 of the IPA vapor generator 11, the nitrogen is injected from the injection nozzle 54 toward the water surface of the cleaning tank 47.

次に、同図(b)に示すように、洗浄槽47内の内部に基板Wを搬入し、基板支持台50に複数枚の基板Wを立位状態に支持し、純水供給ノズル51から純水を供給すると、基板Wは純水によって洗浄される。純水供給ノズル51から純水を供給し続けると、洗浄槽47は純水によって満たされ、オーバフローした純水は、純水オーバフロー槽52に収容される。   Next, as shown in FIG. 4B, the substrate W is carried into the cleaning tank 47, and a plurality of substrates W are supported in a standing state on the substrate support base 50. From the pure water supply nozzle 51, When pure water is supplied, the substrate W is washed with pure water. If pure water is continuously supplied from the pure water supply nozzle 51, the cleaning tank 47 is filled with pure water, and the overflowed pure water is stored in the pure water overflow tank 52.

基板Wの洗浄後、同図(c)に示すように、排液弁48を開弁すると、洗浄槽47内の純水は排液管49から排液される。同時に、IPAベーパー生成装置11によって生成されたIPAベーパーがベーパー供給管26から供給されると、IPAベーパーは噴射ノズル54から洗浄槽47に向かって噴射される。従って、洗浄槽47はIPAベーパー雰囲気となり、基板W上の水滴はIPAと置換される。   After cleaning the substrate W, as shown in FIG. 5C, when the drain valve 48 is opened, the pure water in the cleaning tank 47 is drained from the drain pipe 49. At the same time, when the IPA vapor generated by the IPA vapor generator 11 is supplied from the vapor supply pipe 26, the IPA vapor is injected from the injection nozzle 54 toward the cleaning tank 47. Accordingly, the cleaning tank 47 is in an IPA vapor atmosphere, and water droplets on the substrate W are replaced with IPA.

次に、処理液供給ユニット31のIPA供給弁33bを閉弁し、IPAベーパー生成装置11へのIPAの供給を停止し、窒素のみをIPAベーパー生成装置11へ供給すると、同図(d)に示すように、窒素は瞬時に加熱された後、ベーパー供給管26を介して基板Wに噴射されるため、基板W上のIPAは発散される。このとき、洗浄槽47の下部から有機排気を行なう。   Next, when the IPA supply valve 33b of the treatment liquid supply unit 31 is closed, the supply of IPA to the IPA vapor generator 11 is stopped, and only nitrogen is supplied to the IPA vapor generator 11, FIG. As shown, since the nitrogen is heated instantaneously and then sprayed onto the substrate W through the vapor supply pipe 26, the IPA on the substrate W is emitted. At this time, organic exhaust is performed from the lower part of the cleaning tank 47.

このようにして基板Wの洗浄・乾燥が完了した後、同図(e)に示すように、洗浄槽47を横方向に移動させ、洗浄槽47を開口した後、基板Wを洗浄槽47から搬出する。なお、本実施形態においては、IPAベーパーを供給した後、窒素を供給するようにしたが、薬液を供給したのち、IPAベーパーを供給し、最後に窒素を供給するようにしてもよい。   After the cleaning and drying of the substrate W is completed in this way, the cleaning tank 47 is moved in the horizontal direction and the cleaning tank 47 is opened as shown in FIG. Take it out. In the present embodiment, nitrogen is supplied after the IPA vapor is supplied. However, after supplying the chemical solution, the IPA vapor may be supplied and finally nitrogen may be supplied.

なお、本発明は前記実施形態そのままに限定されるものではなく、実施段階ではその要旨を逸脱しない範囲で構成要素を変形して具体化できる。また、前記実施形態に開示されている複数の構成要素の適宜な組合せにより種々の発明を形成できる。例えば、実施形態に示される全構成要素から幾つかの構成要素を削除してもよい。さらに、異なる実施形態に亘る構成要素を組み合わせてもよい。   Note that the present invention is not limited to the above-described embodiment as it is, and can be embodied by modifying the constituent elements without departing from the scope of the invention in the implementation stage. Moreover, various inventions can be formed by appropriately combining a plurality of constituent elements disclosed in the embodiment. For example, some components may be deleted from all the components shown in the embodiment. Furthermore, the constituent elements over different embodiments may be combined.

本発明の第1の実施形態を示し、ベーパー乾燥装置の概略的構成図。The schematic block diagram of the vapor drying apparatus which shows the 1st Embodiment of this invention. 同実施形態のベーパー乾燥装置の作用説明図。Action | operation explanatory drawing of the vapor drying apparatus of the embodiment. 同実施形態のベーパー乾燥装置の作用説明図。Action | operation explanatory drawing of the vapor drying apparatus of the embodiment. 同実施形態のベーパー乾燥装置の作用説明図。Action | operation explanatory drawing of the vapor drying apparatus of the embodiment. 同実施形態のベーパー乾燥装置の作用説明図。Action | operation explanatory drawing of the vapor drying apparatus of the embodiment. 同実施形態のベーパー乾燥装置の作用説明図。Action | operation explanatory drawing of the vapor drying apparatus of the embodiment. 同実施形態のベーパー乾燥装置の作用説明図。Action | operation explanatory drawing of the vapor drying apparatus of the embodiment. 本発明の第2の実施形態を示し、ベーパー乾燥装置の概略的構成図。The schematic block diagram of the vapor drying apparatus which shows the 2nd Embodiment of this invention. 同実施形態を示し、(a)〜(e)はベーパー乾燥装置の作用説明図。The same embodiment is shown, (a)-(e) is an operation explanatory view of a vapor dryer.

符号の説明Explanation of symbols

11…IPAベーパー生成装置、14…石英ガラス管、26…ベーパー供給管、31…薬液供給ユニット、38…基板載置台、W…基板 DESCRIPTION OF SYMBOLS 11 ... IPA vapor production | generation apparatus, 14 ... Quartz glass tube, 26 ... Vapor supply pipe, 31 ... Chemical solution supply unit, 38 ... Substrate mounting base, W ... Substrate

Claims (3)

基板を支持する洗浄装置と、
複数種類の処理液を選択的に供給する処理液供給ユニットと、
一端側が前記処理液供給ユニットに接続され、他端側に前記洗浄装置に接続されるベーパー供給管を有し、前記処理液供給ユニットから供給された処理液を流通する流通路を有する石英ガラス管と、
前記石英ガラス管の内側に前記流通路と隔離された状態に設けられたロッドヒーターと、
前記石英ガラス管の外側に設けられ、前記ロッドヒーターを加熱し、輻射熱によって前記流通路を流通する前記処理液を加熱あるいは気化して前記ベーパー供給管に導く加熱手段と、
を具備したことを特徴とするベーパー乾燥装置。
A cleaning device for supporting the substrate;
A treatment liquid supply unit that selectively supplies a plurality of kinds of treatment liquids;
A quartz glass tube having a vapor supply pipe connected to the processing liquid supply unit on one end side and a vapor supply pipe connected to the cleaning device on the other end side, and having a flow passage for circulating the processing liquid supplied from the processing liquid supply unit When,
A rod heater provided inside the quartz glass tube so as to be isolated from the flow path;
A heating means provided outside the quartz glass tube, for heating the rod heater, heating or vaporizing the treatment liquid flowing through the flow path by radiant heat, and guiding the treatment liquid to the vapor supply pipe;
A vapor drying apparatus comprising:
前記洗浄装置は、枚葉洗浄装置またはワンバス洗浄装置であり、基板に対して純水を噴射する純水噴射手段を備えていることを特徴とする請求項1記載のベーパー乾燥装置。   2. The vapor drying apparatus according to claim 1, wherein the cleaning device is a single wafer cleaning device or a one-bath cleaning device, and includes pure water injection means for injecting pure water onto the substrate. 前記処理液供給ユニットは、洗浄薬液、IPA液、窒素を選択的に供給する複数の供給弁及び前記石英ガラス管に定量供給する定量供給手段を備えていることを特徴とする請求項1記載のベーパー乾燥装置。   The said process liquid supply unit is provided with the fixed_quantity | feed_rate supply means which supplies a fixed quantity to the said quartz glass tube and the several supply valve which selectively supplies cleaning chemical | medical solution, IPA liquid, and nitrogen. Vapor dryer.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012119388A (en) * 2010-11-29 2012-06-21 Omega Semicon Denshi Kk Superheated steam supply apparatus and substrate processing apparatus

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000121153A (en) * 1998-10-13 2000-04-28 Dainippon Screen Mfg Co Ltd Fluid heater and base processor using it
JP2005327992A (en) * 2004-05-17 2005-11-24 Omega Semicon Denshi Kk Cleaning method and cleaning device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000121153A (en) * 1998-10-13 2000-04-28 Dainippon Screen Mfg Co Ltd Fluid heater and base processor using it
JP2005327992A (en) * 2004-05-17 2005-11-24 Omega Semicon Denshi Kk Cleaning method and cleaning device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012119388A (en) * 2010-11-29 2012-06-21 Omega Semicon Denshi Kk Superheated steam supply apparatus and substrate processing apparatus

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