JPH11186170A - Method and device for forming film - Google Patents

Method and device for forming film

Info

Publication number
JPH11186170A
JPH11186170A JP35273597A JP35273597A JPH11186170A JP H11186170 A JPH11186170 A JP H11186170A JP 35273597 A JP35273597 A JP 35273597A JP 35273597 A JP35273597 A JP 35273597A JP H11186170 A JPH11186170 A JP H11186170A
Authority
JP
Japan
Prior art keywords
reaction
quartz boat
film forming
heating
furnace
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
JP35273597A
Other languages
Japanese (ja)
Other versions
JP3690095B2 (en
Inventor
Shigeru Fujita
繁 藤田
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.)
Sony Corp
Original Assignee
Sony Corp
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 Sony Corp filed Critical Sony Corp
Priority to JP35273597A priority Critical patent/JP3690095B2/en
Publication of JPH11186170A publication Critical patent/JPH11186170A/en
Application granted granted Critical
Publication of JP3690095B2 publication Critical patent/JP3690095B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method and device for forming film by which films can be formed without causing a discharge route to be blocked with by-products left after the films are formed. SOLUTION: A film forming device respectively forms films on objects mounted on a quartz board 14 by introducing a reaction gas to a reaction furnace 13 after the boat 14 is carried in the furnace 13. An electric heater 17 which vaporizes resulted by-products of reaction adhering to the boat 14 by heating the boat 14 on the outside of the furnace 13 after the films are formed is provided on the outside of the furnace 13.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、半導体デバイスの
成膜方法及び成膜装置に関し、特に、成膜処理後に成膜
対象物の支持手段を反応容器の外で加熱し、支持手段に
付着する反応副生成物を気化させて、成膜後に残留する
副生成物により排出経路が詰ってしまうことのない成膜
方法及び成膜装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a film forming method and a film forming apparatus for a semiconductor device, and more particularly, to heating a supporting means for a film forming object outside a reaction vessel after a film forming process and attaching the supporting means to the supporting means. The present invention relates to a film forming method and a film forming apparatus in which a reaction by-product is vaporized and a discharge path is not blocked by a by-product remaining after film formation.

【0002】[0002]

【従来の技術】最近、半導体デバイスを形成する場合の
絶縁膜として、LP−SiN膜が多用されている。この
LP−SiN膜は、縦型減圧CVD装置を用い、反応ガ
スとしてNH3 ガスとSiH2 Cl2 ガスを使用して成
膜するのが一般的である。この場合、成膜の反応は、2
NH3 +SiH2 Cl2 →Si+2NH4 Clとなり、
反応副生成物であるNH4 Cl(塩化アンモニウム)が
発生する。この塩化アンモニウムは、温度が約100℃
以下になると白い粉状になってパーティクル発生或いは
配管詰りの原因となる。従って、この減圧CVD装置に
おいてLP−SiN膜を成膜する場合には、反応炉内に
塩化アンモニウムを入り込ませないようにすることがパ
ーティクル低減のために重要である。
2. Description of the Related Art Recently, an LP-SiN film has been frequently used as an insulating film when a semiconductor device is formed. The LP-SiN film is generally formed using a vertical reduced pressure CVD apparatus and using NH 3 gas and SiH 2 Cl 2 gas as reaction gases. In this case, the reaction of film formation is 2
NH 3 + SiH 2 Cl 2 → Si + 2NH 4 Cl,
NH 4 Cl (ammonium chloride), which is a reaction by-product, is generated. This ammonium chloride has a temperature of about 100 ° C.
Below, it becomes a white powder, causing particles or clogging of piping. Therefore, when forming an LP-SiN film in this low-pressure CVD apparatus, it is important to prevent ammonium chloride from entering the reaction furnace in order to reduce particles.

【0003】ところで、一般のLP−CVD装置におい
ては、成膜処理後の待機状態(スタンバイ状態)で、処
理対象である半導体ウェーハが収納される石英ボートは
反応炉内に挿入されず反応炉外に引き出されているが、
このLP−SiNを形成するCVD装置において、石英
ボートを反応炉外に引き出して待機させた場合、LP−
SiN膜の成膜後に残留し石英ボート下部の石英ボート
台等の形状が複雑な部分に付着したままの塩化アンモニ
ウムが、反応炉外で冷却されて粉状になる。この粉状に
なった塩化アンモニウムは、次の処理工程において反応
炉内に持込まれパーティクル発生源となってしまう。そ
のため、LP−SiNを形成するCVD装置では、石英
ボート下部等に反応副生成物を付着させないようにする
ため、待機時には石英ボートを反応炉内に挿入したまま
にする。
[0003] In a general LP-CVD apparatus, in a standby state (standby state) after a film forming process, a quartz boat in which a semiconductor wafer to be processed is stored is not inserted into the reaction furnace but outside the reaction furnace. Has been drawn to
In this CVD apparatus for forming LP-SiN, when the quartz boat is pulled out of the reaction furnace and is on standby,
Ammonium chloride remaining after the formation of the SiN film and remaining attached to a portion having a complicated shape, such as a quartz boat table below the quartz boat, is cooled outside the reaction furnace to form a powder. The powdered ammonium chloride is carried into the reaction furnace in the next processing step and becomes a particle generation source. Therefore, in a CVD apparatus for forming LP-SiN, the quartz boat is kept inserted in the reaction furnace during standby to prevent reaction by-products from adhering to the lower part of the quartz boat or the like.

【0004】図6に示すように、LP−SiNを形成す
る従来のCVD装置1は、アウタチューブ2aとインナ
チューブ2bからなる反応炉2と、アウタチューブ2a
の周囲に配置されたヒータ3と、アウタチューブ2aと
インナチューブ2bのそれぞれ下端を接続するフランジ
4に設けられた排気管5とを有している。反応炉2内で
成膜処理される複数枚のウェーハ(図示しない)が複数
段に積み重ねて搭載支持される石英ボート6は、石英ボ
ート台7の上に保温筒7aを介して搭載され、成膜処理
時、下端開口を石英ボート台7に閉鎖された反応炉2内
に保温筒7aと共に挿入される。排気管5には、排気用
の真空ポンプ8が接続されている。そして、この石英ボ
ート6を反応炉2内に挿入したままの待機時に、反応炉
2内において大気圧の下N2 フローによるパージが行わ
れる。
[0004] As shown in FIG. 6, a conventional CVD apparatus 1 for forming LP-SiN comprises a reactor 2 comprising an outer tube 2a and an inner tube 2b, and an outer tube 2a.
And an exhaust pipe 5 provided on a flange 4 connecting the lower ends of the outer tube 2a and the inner tube 2b. A quartz boat 6 in which a plurality of wafers (not shown) to be subjected to film formation processing in the reaction furnace 2 are stacked and supported in a plurality of stages is mounted on a quartz boat table 7 via a heat retaining cylinder 7a. At the time of film processing, the lower end opening is inserted together with the heat retaining cylinder 7 a into the reaction furnace 2 closed by the quartz boat table 7. An exhaust vacuum pump 8 is connected to the exhaust pipe 5. When the quartz boat 6 is in a standby state with the quartz boat 6 inserted into the reaction furnace 2, the purge is performed in the reaction furnace 2 by the N 2 flow under the atmospheric pressure.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、石英ボ
ート6を反応炉2内に挿入したままの待機時に、反応炉
2内において大気圧の下N2 フローによるパージが行わ
れると、反応副生成物である塩化アンモニウムによって
排気管5に連通する排出経路が詰ってしまう。即ち、図
7に示すように、N2 ガスによるパージの際、真空ポン
プ8に通じる排気経路の弁が閉じられて反応炉2内は常
圧となり、反応炉2内に送り込まれたN2ガスと待機時
に気化した塩化アンモニウムガスは共に排気ガスとし
て、パージ圧力により排気管5からベントライン9を経
てLP−CVD装置1の外に排出される。その途中、細
い排気配管からなるベントライン9で塩化アンモニウム
による詰りが生じてしまう。
However, when the quartz boat 6 is inserted into the reaction furnace 2 and the purge is performed in the reaction furnace 2 by the N 2 flow under the atmospheric pressure, the reaction by-products are generated. The discharge path communicating with the exhaust pipe 5 is clogged by the ammonium chloride. That is, as shown in FIG. 7, when purging with N 2 gas, the valve of the exhaust path leading to the vacuum pump 8 is closed, the pressure in the reactor 2 becomes normal pressure, and the N 2 gas fed into the reactor 2 is released. And the ammonium chloride gas vaporized during the standby time are both discharged as exhaust gas from the exhaust pipe 5 through the vent line 9 to the outside of the LP-CVD apparatus 1 by the purge pressure. On the way, clogging with ammonium chloride occurs in the vent line 9 composed of a thin exhaust pipe.

【0006】これは、LP−SiN膜の成膜後に反応副
生成物として残留する塩化アンモニウムが石英ボート台
7等の形状が複雑な部分に付着し、それが排気途中で冷
却され粉状になってしまうためである。ベントライン9
が詰ってしまった場合、詰りを解消するために装置のメ
ンテナンスが必要となり、装置のダウンタイムが増加し
て稼働率が低下してしまう。
[0006] This is because ammonium chloride remaining as a reaction by-product after deposition of the LP-SiN film adheres to a portion having a complicated shape such as the quartz boat table 7 and the like, and is cooled to a powdery state during the evacuation. This is because Vent line 9
If clogging occurs, maintenance of the device is required to eliminate the clogging, and the downtime of the device increases, and the operation rate decreases.

【0007】一方、加熱処理中に石英ボート下部等への
反応生成物の付着防止を図った熱処理装置が、特開平5
−291158号公報に開示されている。この熱処理装
置は、「被処理体を水平に複数枚支持する支持体を下方
から挿入する開口部を有し導入される反応ガスにより前
記被処理体の処理が行われる筒状反応容器と、前記筒状
反応容器内を気密に保持する前記開口部の蓋体と、前記
筒状反応容器を包囲して設けられる加熱部とを備えた熱
処理装置において、前記蓋体の前記筒状反応容器内側面
を加熱して反応生成物の付着を防止する加熱装置を設
け」ている。この熱処理装置においては、反応容器の内
側面に設けた加熱装置により反応容器内に支持体(石英
ボート)が搬入されたまま蓋体が加熱され、反応容器の
下方及び蓋体に反応生成物が付着することがないため、
被処理体である半導体ウェーハの汚染源を発生させな
い。
On the other hand, Japanese Patent Application Laid-Open No. Hei 5 (1993) discloses a heat treatment apparatus for preventing reaction products from adhering to the lower part of a quartz boat during heat treatment.
No. 291158. This heat treatment apparatus includes: a tubular reaction vessel having an opening for inserting a support that horizontally supports a plurality of objects to be processed from below, wherein the processing of the object is performed by a reaction gas introduced; In a heat treatment apparatus including: a lid at the opening that keeps the inside of the tubular reaction vessel airtight; and a heating unit provided to surround the tubular reaction vessel, the inside of the tubular reaction vessel of the lid is provided. And a heating device for heating the reaction product to prevent the adhesion of the reaction product. " In this heat treatment apparatus, the lid is heated while the support (quartz boat) is carried into the reaction vessel by a heating device provided on the inner surface of the reaction vessel, and the reaction products are placed below the reaction vessel and on the lid. Because it does not adhere,
It does not generate a contamination source of the semiconductor wafer to be processed.

【0008】しかしながら、この公報記載の熱処理装置
は、反応容器内に装着された石英ボートの下部を加熱し
てボート下部への反応生成物の付着を防止するものであ
り、加熱されたボート下部のガスは反応容器の配管を通
して外部に排出される。従って、排気途中で冷却され粉
状に固化して配管を詰らせるという上記技術的課題を示
唆せず、その解決策は開示されない。
However, the heat treatment apparatus described in this publication heats the lower part of the quartz boat mounted in the reaction vessel to prevent the reaction products from adhering to the lower part of the boat. The gas is discharged to the outside through the piping of the reaction vessel. Therefore, it does not suggest the above-mentioned technical problem of cooling during the evacuation, solidifying into a powdery state, and clogging the piping, and does not disclose a solution thereto.

【0009】本発明は、上記従来技術を考慮してなされ
たものであって、成膜後に残留する副生成物により排出
経路が詰ってしまうことのない成膜方法及び成膜装置の
提供を目的とする。
SUMMARY OF THE INVENTION The present invention has been made in consideration of the above-mentioned prior art, and has as its object to provide a film forming method and a film forming apparatus in which a discharge path is not blocked by a by-product remaining after film forming. And

【0010】[0010]

【課題を解決するための手段】上記目的を達成するた
め、本発明においては、成膜対象を支持手段に搭載し、
この支持手段が搬入された反応容器内に反応ガスを導入
し、前記成膜対象に成膜処理を行う成膜方法において、
成膜処理後に前記支持手段を前記反応容器の外で加熱
し、この支持手段に付着する反応副生成物を気化させる
ことを特徴とする成膜方法を提供する。
In order to achieve the above object, according to the present invention, a film formation target is mounted on a support means,
In the film forming method of introducing a reaction gas into the reaction vessel into which the supporting unit is carried, and performing a film forming process on the film forming target,
A film forming method is provided, wherein the supporting means is heated outside the reaction vessel after the film forming process, and a reaction by-product adhered to the supporting means is vaporized.

【0011】上記構成によれば、成膜終了後、反応容器
から成膜対象を搭載した支持手段が引き出されて反応容
器の外で支持手段の下端が加熱され、支持手段に付着す
る反応副生成物の気化が反応容器の外で行われる。これ
により、成膜後に残留する反応副生成物により反応容器
の排出経路が詰ってしまうことがない。
According to the above construction, after the film formation is completed, the supporting means on which the object to be formed is mounted is pulled out of the reaction vessel, and the lower end of the supporting means is heated outside the reaction vessel, and the reaction by-product adhering to the supporting means is attached. Evaporation of the material takes place outside the reaction vessel. Accordingly, the discharge route of the reaction container is not blocked by the reaction by-product remaining after the film formation.

【0012】また、上記成膜方法を実現するため、本発
明においては、成膜対象を支持手段に搭載し、この支持
手段が搬入された反応容器内に反応ガスを導入し、前記
成膜対象に成膜処理を行う成膜装置において、前記反応
容器の外に設置され、成膜処理後に前記支持手段を前記
反応容器の外で加熱してこの支持手段に付着する反応副
生成物を気化させる加熱手段を備えたことを特徴とする
成膜装置を提供する。
Further, in order to realize the above-mentioned film forming method, in the present invention, a film forming object is mounted on a supporting means, and a reaction gas is introduced into a reaction vessel into which the supporting means is carried. In a film forming apparatus for performing a film forming process, the supporting means is installed outside the reaction vessel after the film forming processing, and the supporting means is heated outside the reaction vessel to vaporize a reaction by-product adhered to the supporting means. A film forming apparatus provided with a heating means is provided.

【0013】[0013]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1は、本発明の実施の形態に係
るLP−SiNを形成する減圧CVD装置の概略説明図
である。図2は、図1の反応炉に挿入された石英ボート
と電熱ヒータを示す説明図である。図3は、図2の電熱
ヒータの加熱による反応副生成物の気化状態の説明図で
ある。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic explanatory view of a low-pressure CVD apparatus for forming LP-SiN according to an embodiment of the present invention. FIG. 2 is an explanatory view showing a quartz boat and an electric heater inserted into the reaction furnace of FIG. FIG. 3 is an explanatory diagram of a vaporized state of a reaction by-product due to heating by the electric heater of FIG.

【0014】図1に示すように、縦型のLP−CVD装
置10は、装置ケース11内の上部に、ヒータ12に覆
われた反応炉(反応容器)13を有し、この反応炉13
の下方に、石英ボート(支持手段)14が配置されてい
る。石英ボート14は、成膜処理対象の半導体ウェーハ
(図示しない)を水平状態に複数枚搭載可能に形成さ
れ、その下端に、保温筒15を介して石英ボート台16
が一体的に装着されている。石英ボート台16は、昇降
機構及び回転機構(図示しない)により自在に昇降及び
回転が可能であり、石英ボート台16の昇降により石英
ボート14は保温筒15とともに反応炉13内に挿入さ
れ或いは反応炉13から引き出される。石英ボート14
及び石英ボート台16は、例えば石英ガラス或いはSi
C等により形成される。
As shown in FIG. 1, a vertical LP-CVD apparatus 10 has a reaction furnace (reaction vessel) 13 covered with a heater 12 at an upper part in an apparatus case 11.
A quartz boat (supporting means) 14 is disposed below. The quartz boat 14 is formed so that a plurality of semiconductor wafers (not shown) to be subjected to a film forming process can be mounted horizontally, and a quartz boat table 16
Are integrally mounted. The quartz boat table 16 can be freely moved up and down and rotated by a lifting mechanism and a rotating mechanism (not shown). It is withdrawn from the furnace 13. Quartz boat 14
The quartz boat table 16 is made of, for example, quartz glass or Si.
C or the like.

【0015】装置ケース11内の底部には、反応炉13
から引き出されてヒータ12の下方に位置する石英ボー
ト14下端の石英ボート台16を取り囲むように、反応
炉13の外に円環状の電熱ヒータ(加熱手段)17が設
置されている。電熱ヒータ17の側方には、半導体ウェ
ーハを石英ボート14に搭載し或いは石英ボート14か
ら取り出すウェーハ搬送機18が設置されている。装置
ケース11の下部外表面には、操作パネル19が設けら
れている。
A reaction furnace 13 is provided at the bottom of the apparatus case 11.
An annular electric heater (heating means) 17 is provided outside the reaction furnace 13 so as to surround the quartz boat table 16 at the lower end of the quartz boat 14 which is drawn out of the heater 12 and located below the heater 12. On the side of the electric heater 17, a wafer transfer machine 18 for mounting a semiconductor wafer on the quartz boat 14 or taking out the semiconductor wafer from the quartz boat 14 is provided. An operation panel 19 is provided on a lower outer surface of the device case 11.

【0016】図2に示すように、ヒータ12に囲まれた
反応炉13は、アウタチューブ20とインナチューブ2
1のそれぞれ下端がフランジ22に接続され、下端が開
口する二重構造の円筒状に形成される。フランジ22に
は、アウタチューブ20とインナチューブ21の間隙を
介して反応炉13内の反応空間に連通する排気管23が
取付けられている。この排気管23は、途中、ベントラ
イン24(図3参照)に分岐後、排気用の真空ポンプ2
5(図3参照)に接続される。
As shown in FIG. 2, a reaction furnace 13 surrounded by a heater 12 includes an outer tube 20 and an inner tube 2.
1 is connected to the flange 22 at the lower end, and is formed in a double-layered cylindrical shape with an open lower end. An exhaust pipe 23 is attached to the flange 22 so as to communicate with a reaction space in the reaction furnace 13 via a gap between the outer tube 20 and the inner tube 21. The exhaust pipe 23 branches off into a vent line 24 (see FIG. 3) on the way, and then is evacuated to a vacuum pump 2.
5 (see FIG. 3).

【0017】石英ボート14の上昇時、保温筒15とと
もに石英ボート14が反応炉13内に挿入状態となり、
フランジ22の下端に石英ボート台16の上面が当接し
て反応炉13の下端開口を閉鎖する。石英ボート14の
下降時、反応炉13の下方に移動した石英ボート14
は、その下端の石英ボート台16が電熱ヒータ17に囲
まれ、電熱ヒータ17への通電により石英ボート台16
が加熱される。
When the quartz boat 14 is raised, the quartz boat 14 is inserted into the reaction furnace 13 together with the heat retaining tube 15,
The upper surface of the quartz boat table 16 contacts the lower end of the flange 22 to close the lower end opening of the reaction furnace 13. When the quartz boat 14 descends, the quartz boat 14 moved below the reactor 13
The quartz boat table 16 at the lower end is surrounded by an electric heater 17, and the electric
Is heated.

【0018】図3に示すように、LP−SiN膜の成膜
終了後、反応炉13から石英ボート14が引き出される
とともに、反応炉13内において大気圧の下N2 フロー
によるパージが行われる。石英ボート14が反応炉13
の外に出ると、反応炉13の下端開口は、反応炉13に
備えられた蓋(図示しない)により塞がれる。石英ボー
ト14が反応炉13の外に出て電熱ヒータ17に囲まれ
た石英ボート台16は、電熱ヒータ17により100℃
以上に加熱された状態で待機する。
As shown in FIG. 3, after the formation of the LP-SiN film is completed, the quartz boat 14 is pulled out of the reaction furnace 13 and the inside of the reaction furnace 13 is purged by the N 2 flow under the atmospheric pressure. Quartz boat 14 is reactor 13
, The lower end opening of the reaction furnace 13 is closed by a lid (not shown) provided in the reaction furnace 13. The quartz boat table 16 in which the quartz boat 14 goes out of the reaction furnace 13 and is surrounded by the electric heater 17 is heated to 100 ° C. by the electric heater 17.
It waits in the state heated above.

【0019】N2 ガスによるパージの際、真空ポンプ2
5に通じる排気経路の弁が閉じられて反応炉13内は常
圧となる。このため、石英ボート14の下降中、N2
スはパージ圧力で反応炉13の下端から反応炉13外に
排出されるが、下端開口が塞がれる石英ボート14の待
機中は、N2 ガスは同様にパージ圧力で排気管23から
ベントライン24へと送り出されLP−CVD装置10
外へと排出される。
When purging with N 2 gas, the vacuum pump 2
The valve in the exhaust path leading to 5 is closed, and the pressure in the reaction furnace 13 becomes normal pressure. Therefore, during the descent of the quartz boat 14, but N 2 gas is discharged to the outside the reactor 13 from the lower end of the reactor 13 at a purge pressure, the waiting quartz boat 14 which the lower end opening is closed, N 2 gas Is similarly sent out from the exhaust pipe 23 to the vent line 24 at the purge pressure and the LP-CVD apparatus 10
It is discharged outside.

【0020】石英ボート台16が加熱されることによ
り、LP−SiN膜の成膜後に反応副生成物として残留
し石英ボート台16等の形状が複雑な部分に付着した塩
化アンモニウム(NH4 Cl)が、塩化アンモニウムガ
スとなって気化・拡散する。この気化・拡散する塩化ア
ンモニウムガスは、石英ボート台16の加熱が反応炉1
3の外で行われるため、反応炉13に連通する排気管2
3に流れ込むことはなく、排気管23を通って排気され
る途中で冷却され粉状になることがない。従って、粉状
になった塩化アンモニウムにより、細い排気配管からな
るベントライン24が詰ることもない。
When the quartz boat table 16 is heated, ammonium chloride (NH 4 Cl) which remains as a reaction by-product after the LP-SiN film is formed and adheres to a portion having a complicated shape such as the quartz boat table 16. Are vaporized and diffused as ammonium chloride gas. The vaporized and diffused ammonium chloride gas is supplied to the reaction vessel 1 by heating the quartz boat table 16.
3, the exhaust pipe 2 communicating with the reactor 13
3 does not flow, and is not cooled and becomes powdery during exhaustion through the exhaust pipe 23. Therefore, the vent line 24 composed of a thin exhaust pipe is not clogged with the powdery ammonium chloride.

【0021】図4は、電熱ヒータの代りに加熱体を用い
た図2と同様の説明図であり、図5は、図4の加熱体の
加熱による反応副生成物の気化状態の説明図である。こ
の例では、加熱手段として電熱ヒータの代りに加熱流体
を循環させる加熱体が用いられる。
FIG. 4 is an explanatory view similar to FIG. 2 in which a heating element is used instead of an electric heater, and FIG. 5 is an explanatory view of a vaporized state of a reaction by-product by heating the heating element in FIG. is there. In this example, a heating element that circulates a heating fluid is used as the heating means instead of the electric heater.

【0022】図4に示すように、加熱体26は、石英ボ
ート台16を埋設状態に載置可能な凹形状に形成され、
導入管27から導入されて排出管28から排出される加
熱流体の循環により石英ボート台16の底面及び側面を
加熱することができる。図5に示すように、LP−Si
N膜の成膜終了後、石英ボート14が下降して石英ボー
ト14が反応炉13の外に出るとともに石英ボート台1
6が加熱体26に載置され、石英ボート台16は加熱体
26により100℃以上に加熱される。
As shown in FIG. 4, the heating element 26 is formed in a concave shape in which the quartz boat table 16 can be placed in a buried state.
The bottom and side surfaces of the quartz boat table 16 can be heated by circulation of the heating fluid introduced from the introduction tube 27 and discharged from the discharge tube 28. As shown in FIG.
After the N film is formed, the quartz boat 14 descends and the quartz boat 14 exits the reaction furnace 13 and the quartz boat table 1
The quartz boat table 16 is heated to 100 ° C. or higher by the heater 26.

【0023】このように、反応炉13の外で石英ボート
台16が加熱されることにより、LP−SiN膜の成膜
後に反応副生成物として残留し石英ボート台16等の形
状が複雑な部分に付着した塩化アンモニウムが、塩化ア
ンモニウムガスとなって気化・拡散する際に、反応炉1
3に連通する排気管23に流れ込むことがない。その他
の構成及び作用効果は前記図2及び図3の実施の形態と
同様である。
As described above, when the quartz boat table 16 is heated outside the reaction furnace 13, the quartz boat table 16 remains as a reaction by-product after the LP-SiN film is formed, and the quartz boat table 16 and the like have complicated shapes. When the ammonium chloride adhering to the gas is vaporized and diffused as ammonium chloride gas, the reaction furnace 1
3 does not flow into the exhaust pipe 23 communicating with the exhaust pipe 3. Other configurations, functions and effects are the same as those of the embodiment shown in FIGS.

【0024】以上、電熱ヒータ17或いは加熱体26に
より、石英ボート台16は反応炉13の外でしか加熱さ
れず、LP−SiN膜の成膜後に反応副生成物として残
留し石英ボート台16等に付着した塩化アンモニウム
は、反応炉13の外で塩化アンモニウムガスとなって気
化・拡散する。従って、パーティクル発生源である塩化
アンモニウムが反応炉13内に入り込まないので、パー
ティクルの低減が可能となり半導体デバイスの品質向上
をもたらす。また塩化アンモニウムにより反応炉13の
排出経路であるベントライン24が詰ることがないの
で、詰りを解消するためのLP−SiNを形成するCV
D装置10のメンテナンス頻度が低減し、装置の稼働率
が向上する。
As described above, the quartz boat table 16 is heated only outside the reaction furnace 13 by the electric heater 17 or the heating element 26, and remains as a reaction by-product after the LP-SiN film is formed, and the quartz boat table 16 and the like are not heated. Ammonium chloride adhered to is vaporized and diffused as an ammonium chloride gas outside the reaction furnace 13. Therefore, since ammonium chloride, which is a particle generation source, does not enter the reaction furnace 13, particles can be reduced and the quality of a semiconductor device can be improved. In addition, since the vent line 24, which is the discharge path of the reaction furnace 13, is not clogged by ammonium chloride, the CV for forming LP-SiN for eliminating the clogging is eliminated.
The maintenance frequency of the D device 10 is reduced, and the operation rate of the device is improved.

【0025】なお、本発明においては、上述した縦型減
圧CVD装置に限らず、横型減圧CVD装置においても
同様の効果が得られる。また、電熱ヒータ17或いは加
熱体26に限らず他の加熱方法により石英ボート台16
を加熱してもよい。
In the present invention, the same effect can be obtained not only in the above-described vertical type low pressure CVD apparatus but also in a horizontal type low pressure CVD apparatus. Further, the quartz boat table 16 is not limited to the electric heater 17 or the heating body 26 but may be formed by another heating method.
May be heated.

【0026】また、SiN膜の成膜に限らず、他の各種
反応ガスを用いた成膜プロセスに適用可能である。ま
た、CVD装置に限らず、アニールや拡散処理等のため
の加熱炉に対しても適用可能である。
The present invention can be applied not only to the formation of the SiN film but also to a film formation process using other various reaction gases. Further, the present invention is not limited to the CVD apparatus, and is applicable to a heating furnace for annealing, diffusion processing, and the like.

【0027】[0027]

【発明の効果】以上説明したように、本発明に係る成膜
方法によれば、成膜終了後、反応容器から成膜対象を搭
載した支持手段が引き出されて反応容器の外で支持手段
の下端が加熱され、支持手段に付着する反応副生成物の
気化が反応容器の外で行われるので、パーティクル発生
源である反応副生成物が反応容器内に入り込まず、パー
ティクルの低減が可能となり半導体デバイスの品質向上
をもたらす。また、反応副生成物により反応容器の排出
経路が詰ることがないので、詰りを解消するための装置
のメンテナンス頻度が低減し、装置の稼働率が向上す
る。
As described above, according to the film forming method of the present invention, after the film formation is completed, the supporting means on which the object to be formed is mounted is pulled out of the reaction vessel, and the supporting means is removed outside the reaction vessel. Since the lower end is heated and the reaction by-products adhering to the supporting means are vaporized outside the reaction vessel, the reaction by-products, which are the source of particles, do not enter the reaction vessel, and the particles can be reduced. Brings improved device quality. In addition, since the reaction by-product does not block the discharge path of the reaction vessel, the frequency of maintenance of the device for eliminating the clogging is reduced, and the operation rate of the device is improved.

【0028】また、本発明に係る成膜装置によれば、上
記成膜方法を実施してその効果を得ることができる。
Further, according to the film forming apparatus of the present invention, the effect can be obtained by performing the above film forming method.

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

【図1】 本発明の実施の形態に係るLP−SiNを形
成する減圧CVD装置の概略説明図。
FIG. 1 is a schematic explanatory view of a low pressure CVD apparatus for forming LP-SiN according to an embodiment of the present invention.

【図2】 図1の反応炉に挿入された石英ボートと電熱
ヒータを示す説明図。
FIG. 2 is an explanatory view showing a quartz boat and an electric heater inserted into the reaction furnace of FIG.

【図3】 図2の電熱ヒータの加熱による反応副生成物
の気化状態の説明図。
FIG. 3 is an explanatory view of a vaporized state of a reaction by-product by heating of the electric heater of FIG. 2;

【図4】 電熱ヒータの代りに加熱体を用いた図2と同
様の説明図。
FIG. 4 is an explanatory view similar to FIG. 2 but using a heating element instead of an electric heater.

【図5】 図4の加熱体の加熱による反応副生成物の気
化状態の説明図。
FIG. 5 is an explanatory diagram of a vaporized state of a reaction by-product due to heating of the heating body in FIG. 4;

【図6】 従来のLP−CVD装置の概略説明図。FIG. 6 is a schematic explanatory view of a conventional LP-CVD apparatus.

【図7】 図6のLP−CVD装置における気化した反
応副生成物の流れを示す説明図。
FIG. 7 is an explanatory view showing the flow of vaporized reaction by-products in the LP-CVD apparatus of FIG. 6;

【符号の説明】[Explanation of symbols]

10:LP−CVD装置、11:装置ケース、12:ヒ
ータ、13:反応炉、14:石英ボート、15:保温
筒、16:石英ボート台、17:電熱ヒータ、18:ウ
ェーハ搬送機、19:操作パネル、20:アウタチュー
ブ、21:インナチューブ、22:フランジ、23:排
気管、24:ベントライン、25:真空ポンプ、26:
加熱体、27:導入管、28:排出管。
10: LP-CVD apparatus, 11: apparatus case, 12: heater, 13: reaction furnace, 14: quartz boat, 15: heat insulating cylinder, 16: quartz boat table, 17: electric heater, 18: wafer transfer machine, 19: Operation panel, 20: outer tube, 21: inner tube, 22: flange, 23: exhaust pipe, 24: vent line, 25: vacuum pump, 26:
Heating body, 27: introduction pipe, 28: discharge pipe.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】成膜対象を支持手段に搭載し、この支持手
段が搬入された反応容器内に反応ガスを導入し、前記成
膜対象に成膜処理を行う成膜方法において、 成膜処理後に前記支持手段を前記反応容器の外で加熱
し、この支持手段に付着する反応副生成物を気化させる
ことを特徴とする成膜方法。
1. A film forming method in which a film formation target is mounted on a support means, a reaction gas is introduced into a reaction vessel into which the support means is carried, and a film formation process is performed on the film formation object. A film forming method, characterized in that the supporting means is heated outside the reaction vessel later, and a reaction by-product adhering to the supporting means is vaporized.
【請求項2】成膜対象を支持手段に搭載し、この支持手
段が搬入された反応容器内に反応ガスを導入し、前記成
膜対象に成膜処理を行う成膜装置において、 前記反応容器の外に設置され、成膜処理後に前記支持手
段を前記反応容器の外で加熱してこの支持手段に付着す
る反応副生成物を気化させる加熱手段を備えたことを特
徴とする成膜装置。
2. A film forming apparatus for mounting a film formation target on a support means, introducing a reaction gas into the reaction vessel into which the support means is carried, and performing a film formation process on the film formation object. And a heating means for heating the supporting means outside the reaction vessel after the film forming process to vaporize a reaction by-product adhered to the supporting means.
【請求項3】前記加熱手段は、電熱ヒータであることを
特徴とする請求項2に記載の成膜装置。
3. The film forming apparatus according to claim 2, wherein said heating means is an electric heater.
【請求項4】前記加熱手段は、加熱流体を循環させる加
熱体であることを特徴とする請求項2に記載の成膜装
置。
4. The film forming apparatus according to claim 2, wherein said heating means is a heating element for circulating a heating fluid.
JP35273597A 1997-12-22 1997-12-22 Deposition method Expired - Fee Related JP3690095B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35273597A JP3690095B2 (en) 1997-12-22 1997-12-22 Deposition method

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Application Number Priority Date Filing Date Title
JP35273597A JP3690095B2 (en) 1997-12-22 1997-12-22 Deposition method

Publications (2)

Publication Number Publication Date
JPH11186170A true JPH11186170A (en) 1999-07-09
JP3690095B2 JP3690095B2 (en) 2005-08-31

Family

ID=18426084

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005531623A (en) * 2002-06-28 2005-10-20 マックス−プランク−ゲゼルシャフト・ツア・フェルデルング・デア・ヴィッセンシャフテン・エー・ファオ Integrated continuous production method of molecular one-component precursors having nitrogen cross-linking function
WO2012086728A1 (en) 2010-12-21 2012-06-28 株式会社渡辺商行 Vaporizer
WO2012118019A1 (en) 2011-02-28 2012-09-07 株式会社渡邊商行 Vaporizer, center rod used therein, and method for vaporizing material carried by carrier gas

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005531623A (en) * 2002-06-28 2005-10-20 マックス−プランク−ゲゼルシャフト・ツア・フェルデルング・デア・ヴィッセンシャフテン・エー・ファオ Integrated continuous production method of molecular one-component precursors having nitrogen cross-linking function
WO2012086728A1 (en) 2010-12-21 2012-06-28 株式会社渡辺商行 Vaporizer
KR20140034123A (en) 2010-12-21 2014-03-19 가부시키가이샤 와타나베 쇼코 Vaporizer
WO2012118019A1 (en) 2011-02-28 2012-09-07 株式会社渡邊商行 Vaporizer, center rod used therein, and method for vaporizing material carried by carrier gas

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