JPS60100423A - Cleaning process of piping - Google Patents
Cleaning process of pipingInfo
- Publication number
- JPS60100423A JPS60100423A JP58207149A JP20714983A JPS60100423A JP S60100423 A JPS60100423 A JP S60100423A JP 58207149 A JP58207149 A JP 58207149A JP 20714983 A JP20714983 A JP 20714983A JP S60100423 A JPS60100423 A JP S60100423A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- piping
- hydrofluoric
- silicide
- heated
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/4401—Means for minimising impurities, e.g. dust, moisture or residual gas, in the reaction chamber
- C23C16/4405—Cleaning of reactor or parts inside the reactor by using reactive gases
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Cleaning In General (AREA)
- Drying Of Semiconductors (AREA)
- Photovoltaic Devices (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はシラン等の珪化物気体または珪化物を含む混合
気体を流す配管の内壁についた汚れを洗浄する方法に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for cleaning dirt attached to the inner wall of a pipe through which a silicide gas such as silane or a mixed gas containing a silicide flows.
半導体製造装置のうち、CVD 、プラズマCVDおよ
びエビクキシャル成長装置に反応性気体として珪化物気
体または珪化物を含む混合気体を用いる場合、それらの
反応性気体をステンレス製等の材質の配管を使用して反
応室まで導いている。この配管の内壁には主に5iOL
などの珪素酸化物が付着し、半導体の製造上問題となっ
てしまった。即ち、半年〜1年の長期使用における微量
の大気のリークにより混入した酸素と珪化物気体との反
応により、内壁に珪素酸化物が付着してしまった。この
ため、この内壁のイリ着物を洗浄、除去し、製造される
半導体装置の特性の向上を図る方法がめられていた。Among semiconductor manufacturing equipment, when silicide gas or a mixed gas containing silicide is used as a reactive gas in CVD, plasma CVD, and evixaxial growth equipment, the reactive gas is transported using piping made of materials such as stainless steel. It leads to the reaction chamber. Mainly 5iOL is used on the inner wall of this pipe.
Silicon oxides such as these have adhered to the surface, causing problems in the manufacture of semiconductors. That is, silicon oxide was deposited on the inner wall due to a reaction between oxygen mixed in due to a trace amount of atmospheric leakage and silicide gas during long-term use of 6 months to 1 year. For this reason, a method has been sought for cleaning and removing the dirt on the inner wall in order to improve the characteristics of the manufactured semiconductor device.
従来より公知の配管の洗浄方法は、珪化物気体または珪
化物を含む混合気体を流す配管を全部数す外し、ステン
レス管、マスフロメーター、ストンプバルブ等、各々の
部品単位に分解し、弗化水素M溶液または弗化水素酸、
硝酸混合溶液を用いて内壁の付着物を除去するものであ
った。この方法は配管を一度分解するため、洗浄に時間
がかかり、かつ弗化水素溶液または弗化水素、硝酸溶液
等の薬品を直接作業者が用いるため、事故の発生率が高
かった。The conventional method for cleaning pipes is to remove all the pipes that flow silicide gas or a mixture containing silicide, disassemble them into parts such as stainless steel pipes, mass flow meters, stomp valves, etc., and then clean them using fluoride. hydrogen M solution or hydrofluoric acid,
A mixed solution of nitric acid was used to remove deposits on the inner walls. In this method, the pipes are disassembled once, which takes time to clean, and the operator directly uses chemicals such as hydrogen fluoride solution, hydrogen fluoride, or nitric acid solution, resulting in a high rate of accidents.
本発明は前記問題に困惑していた発明者達が実験上見つ
けた発見的発明である。The present invention is a heuristic invention discovered through experiments by the inventors who were perplexed by the above problem.
本発明は珪化物気体または珪化物を含む混合気体を流す
配管に無水弗化水素(純度99.9%以上)気体を流し
、さらに洗浄する配管を加熱することを特徴としている
。The present invention is characterized by flowing anhydrous hydrogen fluoride gas (purity of 99.9% or more) through a pipe through which a silicide gas or a mixed gas containing a silicide flows, and further heating the pipe to be cleaned.
本発明は配管の気体導入口に無水弗化水素ボンベを接続
し、その気体を流すだけで配管内壁に付着した珪素酸化
物等を除去できるので、配管の分解、組立が省略できる
ため、半導体製造装置を停止させている時間が短くてす
み、かつ直接に作業者が薬品等に接触しないため安全で
ある。The present invention connects an anhydrous hydrogen fluoride cylinder to the gas inlet of the piping and simply flows the gas to remove silicon oxide, etc. attached to the inner wall of the piping, so disassembly and assembly of the piping can be omitted, making it possible to manufacture semiconductors. It is safe because the time during which the equipment is stopped is short and the operator does not come into direct contact with chemicals.
また、弗化水素気体を配管に流すと同時にその配管全体
を加熱することにより、洗浄能力を高めることができ、
洗浄時間の短縮にもつながる。加P!!)温度は高温に
なるため、その洗浄能力は高められるが、配管に使用さ
れているマスフローコントローラー、ストップバルブ等
の材質、耐熱温度等によって限界がある。一般には15
0 ’Cまで加熱可能である。また100″C以上、1
50 ’Cまでの加熱により、前記の洗浄能方向上の他
に、配管内壁に吸着している酸素、炭素酸化物、空気、
水等の気体または液体を除去できる利点がある。In addition, by flowing hydrogen fluoride gas into the piping and heating the entire piping at the same time, the cleaning ability can be increased.
This also leads to a reduction in cleaning time. KaP! ! ) Since the temperature is high, the cleaning ability can be improved, but there are limits depending on the materials used in the piping, such as the mass flow controller and stop valve, and the heat resistance temperature. Generally 15
It can be heated up to 0'C. Also, 100″C or more, 1
By heating up to 50'C, in addition to the cleaning performance mentioned above, oxygen, carbon oxides, air, etc. adsorbed on the inner wall of the pipe are removed.
It has the advantage of being able to remove gases or liquids such as water.
以下にその実施例を示す。Examples are shown below.
実施例1
第1図はプラズマCVD装置およびガス配管装置(ドー
ピング系)の概略である。Example 1 FIG. 1 is a schematic diagram of a plasma CVD apparatus and a gas piping system (doping system).
図面において、洗浄を行う配管(2)を十分に装置の排
気ポンプ(10)で真空引きを行う。次にバルブ(3)
を閉じ、バルブ(4)を開け、バルブ(4)とガスポン
への繋ぎ口(1)の間に乾燥N2をパージする。この状
態でガスボンへのつなぎ口(1)より現在ついているポ
ンへを取り外し、無水の弗化水素ボンベを取りつける。In the drawing, the pipe (2) to be cleaned is sufficiently evacuated using the exhaust pump (10) of the device. Next, valve (3)
Close the valve (4) and purge dry N2 between the valve (4) and the connection to the gas pump (1). In this state, remove the current plug from the connection port (1) to the gas cylinder and attach an anhydrous hydrogen fluoride cylinder.
次にステンレス管(2)のまわりを隙間なくリボンヒー
ターで覆う。この状態でリボンヒーターに通電し、15
0℃にステンレス管を加熱し、バルブ(4)を閉しバル
ブ(3)を開は無水弗化水素ボンへを開は弗化水素気体
をステンレス管(2)の内部を通過させ、排気処理槽(
12)を通って排気する。3時間弗化水素気体を流した
後、無水弗化水素ボンベを、閉じ、150℃に加熱した
状態でさらに3時間真空排気を行った。Next, cover the stainless steel tube (2) with a ribbon heater without any gaps. In this state, the ribbon heater is energized and 15
Heat the stainless steel pipe to 0°C, close the valve (4), open the valve (3) to pass the hydrogen fluoride gas through the stainless steel pipe (2), and open the valve (3) to pass the hydrogen fluoride gas through the inside of the stainless steel pipe (2) for exhaust treatment. Tank (
12). After flowing hydrogen fluoride gas for 3 hours, the anhydrous hydrogen fluoride cylinder was closed and evacuated for another 3 hours while being heated to 150°C.
この洗浄を行った後、この装置を用いてシラン(Sin
H2*ILn > 1 )の珪化物気体にて公知のプラ
ズマCvD法により太陽電池を作製したところ、洗浄前
は5.5%前後の太陽電池の効率が、本発明の洗浄番行
った後の作製のものでは、8.5%の効率が出るように
なった。また反応室(8)から排気側の配管(2′)も
正禽前は排気ポンプ(1o)の油で汚れていたものがき
れいに洗浄されていた。After this cleaning, silane (Sin
When a solar cell was fabricated by a known plasma CVD method using a silicide gas with H2*ILn > 1), the efficiency of the solar cell was around 5.5% before cleaning, but after the cleaning process of the present invention, the efficiency of the solar cell was approximately 5.5%. With this, the efficiency was 8.5%. In addition, the piping (2') on the exhaust side from the reaction chamber (8), which had previously been contaminated with oil from the exhaust pump (1o), had been cleaned.
本実施例のようにガス配管はまったく大気に触れること
な(洗浄ができるので、ステンレス管内壁に新たに水、
空気、酸素、炭素酸化物の吸着をまったくさせず、半導
体膜特性に影響を与えるC10、N等の不純物濃度を減
らすことができた。As in this example, the gas piping does not come in contact with the atmosphere at all (it can be cleaned, so new water or water is added to the inner wall of the stainless steel pipe).
It was possible to reduce the concentration of impurities such as C10 and N, which affect semiconductor film characteristics, without adsorbing air, oxygen, or carbon oxides at all.
本発明において、弗化水素と同時に純度99.999%
以上(水または酸素加物が3PPM以下)の不活性気体
であるマルゴン、窒素、水素、ヘリュームを不活性気体
によりパージ(排気処理)を行うことは有効である。In the present invention, hydrogen fluoride and at the same time have a purity of 99.999%.
It is effective to purge (exhaust treatment) the above inert gases (water or oxygen additives are 3 PPM or less) such as margon, nitrogen, hydrogen, and helium with an inert gas.
第1図はプラズマCVD装置の概要とガス配管を示す。
第2図はガス配管にリボンヒーターをまいた時の断面を
示す。
1はガスボンベ導入口、2.2′はステンレス管を示す
。
特許出願人
特許庁長官 殿
1.事件の表示
昭和58年特許願第207149号
26発明の名称
配管の洗浄方法
3、Ht1正をする者
4、補正命令の日付
昭和59年1月11日
(発送日 昭和59年1月31日)
5、補正の対象
図面の簡単な説明の欄
6、補正の内容
明細書第6頁第9行目から第6頁第12行までを削除す
る。FIG. 1 shows an outline of the plasma CVD apparatus and gas piping. Figure 2 shows a cross section when ribbon heaters are placed on gas piping. 1 is a gas cylinder inlet, and 2.2' is a stainless steel pipe. Patent applicant Commissioner of the Patent Office 1. Display of the case 1982 Patent Application No. 207149 26 Name of the invention Method for cleaning pipes 3, Person who makes Ht1 correction 4, Date of amendment order January 11, 1980 (Shipping date January 31, 1980) 5. Delete column 6 for the brief description of the drawing to be corrected, and from line 9 on page 6 to line 12 on page 6 of the specification of contents of the correction.
Claims (1)
を流す配管に無水弗化水素(肝)ガスを流すことによっ
て、配管を分解することなく、その配管内壁の汚れを除
去することを特徴とする配管の洗浄方法。 2、特許請求の範囲第1項において、洗浄をしようとす
る配管を加熱することを特徴とする配管の洗浄方法。 3、特許請求の範囲第1項において、使用する無水弗化
水素ば純度99.9%以上のものであることを特徴とす
る配管の洗浄方法。[Claims] 1. By flowing anhydrous hydrogen fluoride (liver) gas through a pipe that flows a silicide gas such as silane and a mixed gas containing a silicide, stains on the inner wall of the pipe can be removed without disassembling the pipe. A method for cleaning piping characterized by removing. 2. A method for cleaning piping according to claim 1, characterized in that the piping to be cleaned is heated. 3. A method for cleaning piping according to claim 1, characterized in that the anhydrous hydrogen fluoride used has a purity of 99.9% or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58207149A JPS60100423A (en) | 1983-11-04 | 1983-11-04 | Cleaning process of piping |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58207149A JPS60100423A (en) | 1983-11-04 | 1983-11-04 | Cleaning process of piping |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60100423A true JPS60100423A (en) | 1985-06-04 |
Family
ID=16535021
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58207149A Pending JPS60100423A (en) | 1983-11-04 | 1983-11-04 | Cleaning process of piping |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60100423A (en) |
-
1983
- 1983-11-04 JP JP58207149A patent/JPS60100423A/en active Pending
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