JPH03229414A - Thermal treatment apparatus - Google Patents

Thermal treatment apparatus

Info

Publication number
JPH03229414A
JPH03229414A JP2025672A JP2567290A JPH03229414A JP H03229414 A JPH03229414 A JP H03229414A JP 2025672 A JP2025672 A JP 2025672A JP 2567290 A JP2567290 A JP 2567290A JP H03229414 A JPH03229414 A JP H03229414A
Authority
JP
Japan
Prior art keywords
exhaust pipe
drain
waste liquid
steam
trap
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2025672A
Other languages
Japanese (ja)
Other versions
JP2668023B2 (en
Inventor
Junichi Kakizaki
柿崎 純一
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tokyo Electron Sagami Ltd
Original Assignee
Tokyo Electron Sagami Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tokyo Electron Sagami Ltd filed Critical Tokyo Electron Sagami Ltd
Priority to JP2025672A priority Critical patent/JP2668023B2/en
Priority to KR1019910001136A priority patent/KR0147044B1/en
Priority to US07/644,565 priority patent/US5088922A/en
Publication of JPH03229414A publication Critical patent/JPH03229414A/en
Application granted granted Critical
Publication of JP2668023B2 publication Critical patent/JP2668023B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

PURPOSE:To reduce variation between wafers subjected to a batch treatment and improve a utilization factor by a method wherein a first exhaust pipe which is provided vertically and a second exhaust pipe which links the first exhaust pipe with a treatment chamber are provided and a drain trap is provided beneath the first exhaust pipe. CONSTITUTION:The temperature of a uniformly heating region in a processing tube 10 is set at, for instance, 1000 deg.C by a heater 16. when steam and HCl gas are supplied to the processing tube 10 to subject a semiconductor wafer to an oxidation treatment, most parts of the steam and HCl gas are exhausted through the tube 10 and the steam is cooled on the inner wall of an exhaust pipe 22 which is provided vertically and drain containing HCl adheres to the inner wall of the exhaust pipe 22 and flows downward along the inner wall of the exhaust pipe 22 into a drain trap 40 and the drain is stored in a drain sink 42. If the level of the drain exceeds the level of holes 44, the drain overflows the drain sink 42 and is discharged from the drain trap 40. Therefore, however large the quantity of the drain is, the first exhaust pipe 22 and a second exhaust pipe 21 are not choked up by the drain, so that a desirable oxidation treatment which eliminates variation between the treated wafers can be realized.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は熱処理装置に関する。[Detailed description of the invention] [Purpose of the invention] (Industrial application field) The present invention relates to a heat treatment apparatus.

(従来の技術) 近年、半導体製造熱処理工程においては、処理ウェハサ
イズが4インチから6インチさらには8インチと大型化
し、バッチ処理するウェハ枚数も100枚から150枚
と増加しており、これら処理容量の増大にともない酸化
や拡散等の熱処理装置から排気管に排出される排気ガス
とともに廃液も増大している。
(Prior art) In recent years, in the heat treatment process of semiconductor manufacturing, the size of processed wafers has increased from 4 inches to 6 inches and even 8 inches, and the number of wafers processed in batches has increased from 100 to 150. As the capacity increases, the amount of waste liquid as well as the exhaust gas discharged from heat treatment equipment such as oxidation and diffusion into the exhaust pipe is increasing.

熱処理装置の中でも特に水蒸気酸化装置ではウェハ処理
後の水蒸気が排気管内で冷やされ多量の廃液が排気管内
に付着する。
Among heat treatment apparatuses, particularly in steam oxidation apparatuses, steam after wafer processing is cooled in an exhaust pipe, and a large amount of waste liquid adheres to the exhaust pipe.

排気ガス中に含まれる反応生成物を排気管内にて捕獲す
るものとして特願昭63−21.1769号公報がある
Japanese Patent Application No. 63-21.1769 discloses a method for capturing reaction products contained in exhaust gas in an exhaust pipe.

半導体基板現像処理装置の廃液処理については特開昭6
1−160933号公報がある。
For waste liquid treatment of semiconductor substrate processing equipment, see Japanese Patent Application Laid-Open No. 6
There is a publication No. 1-160933.

(発明が解決しようとする課題) 水蒸気酸化装置では排気管内に付着した多量の廃液が排
気管内に溜まり、排気管開口が実質的に狭くなり、処理
容器内の排気が十分にできず所望の熱処理ができなくな
り、バッチ処理されるウェハ間のバラツキが大きくなる
改善点を有する。
(Problem to be Solved by the Invention) In a steam oxidation device, a large amount of waste liquid adhering to the inside of the exhaust pipe accumulates in the exhaust pipe, and the opening of the exhaust pipe becomes substantially narrow, making it impossible to exhaust the inside of the processing container sufficiently, resulting in the desired heat treatment. However, there is an improvement in that the wafers that are processed in batches become more inconsistent.

また、定期的に排気管を分解洗浄する必要があり熱処理
装置の稼動率を低下させている。
Furthermore, it is necessary to periodically disassemble and clean the exhaust pipe, which reduces the operating rate of the heat treatment apparatus.

反応生成物を捕獲する前者の文献の技術は多量の廃液を
溜めることができないため定期的にトラツブ部分を分解
洗浄する必要があり装置の稼動率を低下させている。廃
液処理を行う後者の文献の技術は排気管内の管壁に多量
の廃液が付着する酸化装置等においては、廃液を十分に
集めることができず、排気管内に廃液が溜まり排気管開
口が実質的に狭くなり前記と同様の問題が起る。さらに
酸化や拡散等の装置においては、高温の排気ガスやHC
R等の腐食性ガスが排出されるので、熱による変形やガ
スによる腐食の問題点を有する。
The former technique disclosed in the literature, which captures reaction products, cannot store a large amount of waste liquid, and therefore requires periodic disassembly and cleaning of the trap portion, which reduces the operating rate of the device. The technology in the latter document for waste liquid treatment cannot collect enough waste liquid in oxidizers etc. where a large amount of waste liquid adheres to the pipe wall in the exhaust pipe, and the waste liquid accumulates in the exhaust pipe, effectively closing the exhaust pipe opening. The same problem as above occurs. Furthermore, in equipment such as oxidation and diffusion, high temperature exhaust gas and HC
Since corrosive gases such as R are discharged, there are problems of deformation due to heat and corrosion due to gas.

この発明は、上記点に鑑みなされたもので、バッチ処理
ウェハ間のバラツキが少なく稼動率の高い熱処理装置を
提供することにある。
The present invention has been made in view of the above points, and it is an object of the present invention to provide a heat treatment apparatus that has a high operating rate with little variation among batch-processed wafers.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段) この発明は熱処理後の排ガスを排気管を介して排気する
機構を有する熱処理装置において、上記排気管に垂直に
配置された第1の排気管部と、上記排気管と処理容器を
連結する第2の排気管部を設け、上記第1の排気管部の
下方に位置して廃液トラップを設けるように構成したも
のである。
(Means for Solving the Problems) The present invention provides a heat treatment apparatus having a mechanism for exhausting exhaust gas after heat treatment through an exhaust pipe, including a first exhaust pipe section disposed perpendicularly to the exhaust pipe, and a first exhaust pipe section disposed perpendicularly to the exhaust pipe; A second exhaust pipe section connecting the pipe and the processing container is provided, and a waste liquid trap is provided below the first exhaust pipe section.

(作 用) この発明は排気路に垂直に配置された熱処理後の排ガス
が流通する第1の排気管部を設け、この排気管の内壁に
付着した廃液が廃液トラップに流り込み、上記廃液トラ
ップに溜まった廃液は排気管内と大気間の圧力差を保っ
たまま常時溢れ出るようにして排気路の目づまりを防止
し、処理の安定化を可能にしたものである。
(Function) The present invention provides a first exhaust pipe section which is disposed perpendicularly to the exhaust passage and through which exhaust gas after heat treatment flows, and the waste liquid adhering to the inner wall of this exhaust pipe flows into the waste liquid trap. The waste liquid accumulated in the trap constantly overflows while maintaining the pressure difference between the inside of the exhaust pipe and the atmosphere, thereby preventing clogging of the exhaust pipe and making it possible to stabilize the process.

(実施例) 以下、本発明を縦型酸化炉に適用した一実施例について
図面を参照して具体的に説明する。
(Example) Hereinafter, an example in which the present invention is applied to a vertical oxidation furnace will be specifically described with reference to the drawings.

第1図において縦型のプロセスチューブ10は耐熱性材
料例えば石英チューブからなり、このチューブの一端部
にプロセスガス導入管12を連結し。
In FIG. 1, a vertical process tube 10 is made of a heat-resistant material, such as a quartz tube, and a process gas introduction pipe 12 is connected to one end of the tube.

他端部に排出管13を設けである。A discharge pipe 13 is provided at the other end.

上記排出管13は水平に配置した第2の排気管21を介
して主筒を垂直に配置した第1の排気管22に結合して
おり、この第1の排気管22の上端には排気ファン20
が連結されている。
The exhaust pipe 13 is connected to a first exhaust pipe 22 in which the main cylinder is arranged vertically via a second exhaust pipe 21 arranged horizontally, and an exhaust fan is provided at the upper end of the first exhaust pipe 22. 20
are connected.

上記プロセスチューブ10の周囲には筒状ヒータ16例
えば抵抗加熱ヒータが設けられ、プロセスチューブ10
を所定の温度例えば800℃〜1200℃の範囲で適宜
設定可能としている。
A cylindrical heater 16, for example, a resistance heater, is provided around the process tube 10.
can be appropriately set at a predetermined temperature, for example, in the range of 800°C to 1200°C.

そしてこのプロセスチューブ10内には被処理体として
多数枚のウェハ18を例えば石英製のウェハボート17
上に水平にして収納し、このボート17を載置台19上
に設置し、この載置台19を蓋体14に設置して収納さ
れている。
In this process tube 10, a large number of wafers 18 are placed as objects to be processed, for example, in a wafer boat 17 made of quartz.
The boat 17 is stored horizontally on top, and the boat 17 is installed on a mounting table 19, and this mounting table 19 is installed on the lid body 14 and stored.

上記蓋体14は図示しない昇降機構により上下移動する
ことができ、プロセスチューブ10内の予め定められた
位置にウェハ18を搬入搬出可能な如く構成している。
The lid 14 can be moved up and down by a lifting mechanism (not shown), and is configured so that the wafer 18 can be carried in and out of the process tube 10 at a predetermined position.

前記導入管12には水蒸気発生源2から水蒸気と、マス
フローコントローラ4から)lc4ガスを供給する。
Steam from the steam generation source 2 and LC4 gas (from the mass flow controller 4) are supplied to the introduction pipe 12.

第1の排気管22と第2の排気管21の接続点下方に廃
液トラップ40を配置する。この廃液トラップ40の詳
細については第2図を参照して次に説明する。
A waste liquid trap 40 is arranged below the connection point between the first exhaust pipe 22 and the second exhaust pipe 21. The details of this waste liquid trap 40 will be explained next with reference to FIG.

廃液トラップ40の一部を構成する上記第1の排気管2
2の延長して位置する配管43を液溜め部42の内側に
挿入配置し、上記液溜め部42の上部には穴部44を複
数設け、廃液48を上記穴部44から溢れ出る様に構成
し、液溜め部42の周囲は外側ケース46で密閉してい
る。
The first exhaust pipe 2 forming part of the waste liquid trap 40
A pipe 43 extending from No. 2 is inserted inside the liquid reservoir 42, and a plurality of holes 44 are provided in the upper part of the liquid reservoir 42, so that the waste liquid 48 overflows from the holes 44. However, the periphery of the liquid reservoir 42 is sealed with an outer case 46.

高温ガスや)ICρ等の腐食性ガスと接触する配管43
部分は、非金属例えば石英やふっ素樹脂等の耐熱耐食性
部材から構成されている。
Piping 43 that comes into contact with corrosive gas such as high temperature gas and ICρ
The portion is made of a heat-resistant and corrosion-resistant material such as non-metallic material such as quartz or fluororesin.

液溜め部42や外側ケース46も耐食性部材で構成して
いる。
The liquid reservoir 42 and the outer case 46 are also made of corrosion-resistant materials.

次に上記実施例装置の作用について説明する。Next, the operation of the apparatus of the above embodiment will be explained.

ヒータ16によりプロセスチューブ10内の均熱領域を
例えば1000℃の温度に設定し、水蒸気とH(4ガス
をプロセスチューブ10に供給し半導体ウェハの酸化処
理を行う場合、水蒸気とHC4ガスの多くはプロセスチ
ューブ10を通過して排気され垂直に配置された排気管
22の内壁で水蒸気が冷やされHCQを含んだ廃液が排
気管22の内壁に付着し、排気管22の内壁に沿って落
下し、廃液トラップ40に流れ込み液溜め部42に廃液
が溜められる。なお必要に応じて排気管22の外囲気に
冷却手段を設けても良い。穴部44以上に溜まった廃液
は液溜め部42から溢れ出し、廃液トラップ40から排
出される。
When the soaking area in the process tube 10 is set to a temperature of, for example, 1000°C using the heater 16 and water vapor and H4 gas are supplied to the process tube 10 to perform oxidation treatment on semiconductor wafers, most of the water vapor and H4 gas are The water vapor is exhausted through the process tube 10 and cooled on the inner wall of the vertically arranged exhaust pipe 22, and the waste liquid containing HCQ adheres to the inner wall of the exhaust pipe 22 and falls along the inner wall of the exhaust pipe 22. The waste liquid flows into the waste liquid trap 40 and is stored in the liquid reservoir 42.If necessary, a cooling means may be provided in the outer atmosphere of the exhaust pipe 22.The waste liquid accumulated above the hole 44 overflows from the liquid reservoir 42. and discharged from the waste liquid trap 40.

水平に配置された排気管21部分は100℃以上の温度
であるため廃液は付着しない。
Since the horizontally arranged exhaust pipe 21 has a temperature of 100° C. or higher, no waste liquid adheres thereto.

したがってどの様に廃液が多くても廃液によって、第1
の排気管22や第2の排気管21は塞がれることはなく
、処理ウェハ間のバラツキのない所望の酸化処理を行う
ことができる。
Therefore, no matter how much waste liquid there is, the first
The exhaust pipe 22 and the second exhaust pipe 21 are not blocked, and the desired oxidation process can be performed without variation among processed wafers.

また廃液トラップ40に溜まった廃液は排気管内と大気
間の圧力差を保ったまま常時溢れ出るように構成されて
いるため酸化装置を止めることなく廃液を常時徘呂する
ことができる。
In addition, since the waste liquid accumulated in the waste liquid trap 40 is configured to always overflow while maintaining the pressure difference between the inside of the exhaust pipe and the atmosphere, the waste liquid can be constantly circulated without stopping the oxidizer.

したがって排気管21及び排気管22に廃液が溜まらな
いため定期的に排気管21や排気管22を分解洗浄する
必要がなく酸化装置の稼動率を低下させることがない。
Therefore, since waste liquid does not accumulate in the exhaust pipes 21 and 22, there is no need to periodically disassemble and clean the exhaust pipes 21 and 22, and the operating rate of the oxidizer does not decrease.

また、HCQ等の廃食性ガスを流しても廃液トラップ4
0は非金属の耐食性部材で構成されているため、腐食は
起らない。
In addition, even if waste edible gas such as HCQ is passed, the waste liquid trap 4
0 is constructed from non-metallic corrosion-resistant members, so corrosion does not occur.

また、高温の排気ガスが流されても廃液トラップ40は
石英やふっ素樹脂等で構成されており熱的変形等の問題
は起らない。廃液トラップ40部分の材質は、温度が1
40℃以下の場合2ふっ化樹脂、140〜260℃の場
合4ふっ化樹脂、260℃以上の場合石英等と温度によ
って使いわけても良い。
Further, even if high-temperature exhaust gas is flowed, the waste liquid trap 40 is made of quartz, fluororesin, or the like, so problems such as thermal deformation do not occur. The material of the waste liquid trap 40 has a temperature of 1
Depending on the temperature, di-fluorinated resin may be used at temperatures below 40°C, tetra-fluorinated resin may be used at temperatures between 140 and 260°C, and quartz may be used at temperatures above 260°C.

外側ケース46は100℃以下なので、透明塩化ビニー
ル樹脂を用いれば廃液の溜まり状態を目視チエツクする
ことができる。排気管21部分の温度が100℃以下に
なる場合、廃液が付着するのでプロセスチューブ10に
接続される排気管21は廃液トラップ40に対して若干
下向きに傾斜させ、排気管21に付着した廃液は全て廃
液トラップ40に集められる構成とすることが望ましい
Since the temperature of the outer case 46 is 100° C. or lower, if transparent vinyl chloride resin is used, it is possible to visually check the state of waste liquid accumulation. When the temperature of the exhaust pipe 21 becomes 100°C or less, waste liquid will adhere to it. Therefore, the exhaust pipe 21 connected to the process tube 10 is tilted slightly downward with respect to the waste liquid trap 40, and the waste liquid adhering to the exhaust pipe 21 is removed. It is desirable that all of the liquid is collected in the waste liquid trap 40.

尚、本発明は前記実施例に限定されるものではなく、本
発明の要旨の範囲内で種々の変形実施が可能である。廃
液トラップの形状はU字配管等の形状でも良いことはも
ちろんである。
Note that the present invention is not limited to the above-mentioned embodiments, and various modifications can be made within the scope of the gist of the present invention. Of course, the shape of the waste liquid trap may be a U-shaped pipe or the like.

前記実施例では水蒸気酸化炉について説明を行ったが拡
散炉や常圧CVC装置等の熱処理装置やその他のバッチ
処理装置に応用しても良く、排気管内に流れる排気ガス
も水蒸気に限らず他の処理ガスでも良いことはもちろん
である。また、縦型装置に限らず横型熱処理炉等の横型
装置に適用できるのは当然のことである。
In the above embodiment, a steam oxidation furnace was explained, but it may be applied to heat treatment equipment such as a diffusion furnace or normal pressure CVC equipment, or other batch processing equipment, and the exhaust gas flowing in the exhaust pipe is not limited to steam. Of course, a processing gas may also be used. It goes without saying that the present invention can be applied not only to vertical devices but also to horizontal devices such as horizontal heat treatment furnaces.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明によれば排気管内に廃液が
溜まり排気管が実質的に狭くなることがないため、処理
時の処理ウェハ間のバラツキが発生せず、また装置を止
めることなく常時廃液を排出することができるので装置
の稼動率を向上させられると言う顕著な効果がある。
As explained above, according to the present invention, waste liquid does not accumulate in the exhaust pipe and the exhaust pipe does not become substantially narrow, so there is no variation between processed wafers during processing, and the equipment can be operated at all times without stopping. This has the remarkable effect of improving the operating rate of the device since waste liquid can be discharged.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明に係る縦型熱処理装置の一実施例説明図
、第2図は第1図の廃液トラップ部を拡大して示す説明
図である。 10・・プロセスチューブ 16・・・ヒータ】8・・
・ウェハ      20・・排気ファン21  第2
の排気管   22・・・第1の排気管40・廃液トラ
ップ   42・液溜め部44・・穴部
FIG. 1 is an explanatory diagram of one embodiment of the vertical heat treatment apparatus according to the present invention, and FIG. 2 is an explanatory diagram showing an enlarged view of the waste liquid trap section of FIG. 1. 10...Process tube 16...Heater】8...
・Wafer 20 ・・Exhaust fan 21 2nd
Exhaust pipe 22...first exhaust pipe 40, waste liquid trap 42, liquid reservoir 44...hole

Claims (1)

【特許請求の範囲】[Claims] 熱処理後の排ガスを排気管を介して排気する機構を有す
る熱処理装置において、上記排気管に垂直に配置された
第1の排気管部と、上記排気管と処理容器を連結する第
2の排気管部を設け、上記第1の排気管部の下方に位置
して廃液トラップを設けたことを特徴とする熱処理装置
In a heat treatment apparatus having a mechanism for exhausting exhaust gas after heat treatment through an exhaust pipe, a first exhaust pipe section is arranged perpendicularly to the exhaust pipe, and a second exhaust pipe connects the exhaust pipe and the processing container. A heat treatment apparatus characterized in that a waste liquid trap is provided below the first exhaust pipe section.
JP2025672A 1990-01-23 1990-02-05 Heat treatment equipment Expired - Lifetime JP2668023B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP2025672A JP2668023B2 (en) 1990-02-05 1990-02-05 Heat treatment equipment
KR1019910001136A KR0147044B1 (en) 1990-01-23 1991-01-23 Heat treatment apparatus having exhaust system
US07/644,565 US5088922A (en) 1990-01-23 1991-01-23 Heat-treatment apparatus having exhaust system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2025672A JP2668023B2 (en) 1990-02-05 1990-02-05 Heat treatment equipment

Publications (2)

Publication Number Publication Date
JPH03229414A true JPH03229414A (en) 1991-10-11
JP2668023B2 JP2668023B2 (en) 1997-10-27

Family

ID=12172277

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2025672A Expired - Lifetime JP2668023B2 (en) 1990-01-23 1990-02-05 Heat treatment equipment

Country Status (1)

Country Link
JP (1) JP2668023B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5445521A (en) * 1993-05-31 1995-08-29 Tokyo Electron Kabushiki Kaisha Heat treating method and device
JPH11233505A (en) * 1998-02-13 1999-08-27 Tokyo Electron Ltd Exhaust apparatus
JP2019161130A (en) * 2018-03-16 2019-09-19 株式会社東芝 Film deposition device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0238468U (en) * 1988-08-31 1990-03-14

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0238468U (en) * 1988-08-31 1990-03-14

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5445521A (en) * 1993-05-31 1995-08-29 Tokyo Electron Kabushiki Kaisha Heat treating method and device
JPH11233505A (en) * 1998-02-13 1999-08-27 Tokyo Electron Ltd Exhaust apparatus
JP2019161130A (en) * 2018-03-16 2019-09-19 株式会社東芝 Film deposition device

Also Published As

Publication number Publication date
JP2668023B2 (en) 1997-10-27

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